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US8647289B2 - System and method for optimized apheresis draw and return - Google Patents

System and method for optimized apheresis draw and return Download PDF

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Publication number
US8647289B2
US8647289B2 US13/076,882 US201113076882A US8647289B2 US 8647289 B2 US8647289 B2 US 8647289B2 US 201113076882 A US201113076882 A US 201113076882A US 8647289 B2 US8647289 B2 US 8647289B2
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blood
draw
return line
pressure
blood component
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US20110178453A1 (en
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Etienne Pagès
Michael Ragusa
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Haemonetics Corp
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Haemonetics Corp
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Publication of US20110178453A1 publication Critical patent/US20110178453A1/en
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
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    • A61M1/16Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis with membranes
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    • A61M1/0245Means for controlling the quantity of transfused blood, e.g. by weighing the container and automatic stopping of the transfusion after reaching a determined amount combined with blood container shaking means
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Definitions

  • the present invention relates to systems and methods for blood apheresis and particularly to systems and methods for optimized apheresis draw and return.
  • Apheresis is a procedure in which an individual blood component can be separated and collected from whole blood withdrawn from a subject.
  • whole blood is withdrawn through a needle inserted into the subject's arm and transferred into a cell separator, such as a centrifugal bowl.
  • a cell separator such as a centrifugal bowl.
  • the whole blood is separated into its various components (e.g., plasma, red blood cells, and platelets)
  • one or more of the components can be collected from the centrifugal bowl.
  • the remaining components can be returned to the subject along with a compensation fluid to make up for the volume of the removed component.
  • the technician While performing apheresis procedures, the technician must balance the procedure time with the safety of the patient. In particular, the technician must perform the procedure as quickly as possible to minimize the procedure time and associated discomfort of the subject, but must always be conscious of the safety of the subject.
  • One such area for safety concern is the pressure at which the whole blood is withdrawn from the subject and the remaining blood components are returned to the subject. The pressure at which the remaining components and potential compensation fluid are returned to the subject is critical to the safety of the subject. If the pressure is too high during the return or too low in during the draw, the subject is at risk for vein lesions.
  • Embodiments of the present invention precisely determine donor vein pressure without the need for a sensor to be located within the vein.
  • pressure may be measured at two points within the line or lines that fluidly connect the needle tip to the apheresis device.
  • the two measurement points (P 1 and P 2 ) may be located a distance away from the needle tip within the donor vein.
  • the measurement points may delimit two portions of a line(s) having a known fluid resistance R 1 and R 2 .
  • R may be defined as the change in pressure between the two pressure measurement points divided by a flow rate and may be expressed in mmHg/ml/min.
  • the two portions may include the portion of the line between the needle tip and the first point of measurement and the portion between the first and the second points of measurement.
  • a blood processing device for collecting and exchanging blood components includes a venous-access device for drawing whole blood from a subject and returning unused/uncollected blood components and potential compensation fluid to the subject, and a blood component separation device.
  • the blood component separation device e.g., a centrifuge bowl
  • the blood component separation device may also send the second blood component to a second blood component storage container.
  • the blood processing device may also have a return line fluidly connecting the venous-access device and the blood component separation device.
  • the system may use the return line to return the first blood component to the subject.
  • the system may also have a first and second pressure sensor located on the return line.
  • the first pressure sensor may be located between the blood component separation device and the venous-access device and may determine a first pressure within the return line.
  • the second pressure sensor may be located between the first pressure sensor and the venous-access device and may determine a second pressure within the return line.
  • a pump connected to the return line may control a return flow rate within the return line based on a subject access pressure determined using the first pressure and the second pressure.
  • the subject access pressure may be determined in real time.
  • the system may also have an anticoagulation line for introducing anticoagulant into the drawn blood near the venous-access device.
  • the system may include a valve, located on the return line between the blood component separation device and the venous access device. The valve may stop the flow within the return line.
  • the system may also have an interlock that stops the withdrawal of whole blood from the subject when the system is returning the first blood component to the subject.
  • the subject access pressure may also be based on at least one characteristic of a first portion of the return line and at least one characteristic of a second portion of the return line.
  • the first portion may be between the first and second pressure sensors.
  • the second portion may be between the second pressure sensor and the venous-access device.
  • the characteristics of the first and second portions of the return line may include, but are not limited to, the length, inner diameter, resistance to flow, and materials of construction.
  • the system may also control the return flow rate based on the flow resistances within the first and second portions of the return line. The flow resistances may be calculated based on the line characteristics discussed above.
  • the blood component separation device may further separate the drawn blood into a third blood component in addition to the first blood component and the second blood component.
  • the first blood component may be red blood cells
  • the second blood component may be platelets
  • the third blood component may be plasma.
  • a method of collecting and exchanging blood components using blood processing equipment includes inserting a venous-access device into a subject, and withdrawing whole blood from the subject.
  • the venous-access device may be fluidly connected to a blood separation device in which the drawn blood is collected.
  • the method then separates the withdrawn blood into a first blood component and a second blood component using the blood component separation device, and extracts the second blood component from the blood component separation device.
  • the system or method may return the remaining components (e.g., the first blood component) to the subject through a return line.
  • the method may measure a first pressure within the return line using a first pressure sensor, and a second pressure within the return line using a second pressure sensor.
  • the first and second pressure sensors may be located on the return line.
  • the first pressure sensor may be located on the return line between the venous-access device and the blood component separation device
  • the second pressure sensor may be located on the return line between the venous-access device and the first pressure sensor.
  • the method may then control a return flow rate within the return fluid line based on a subject access pressure that is determined using the first pressure and the second pressure.
  • the subject access pressure may also be determined using at least one characteristic of a first portion of the return line and at least one characteristic of a second portion of the return line.
  • the first portion is between the first and second pressure sensors, and the second portion is between the second pressure sensor and the venous-access device.
  • the characteristics of the line portions can include the length, inner diameter, and materials of construction.
  • the flow rate may also be controlled based on a first flow resistance within the first and/or second portion of the return line. The flow resistances may be calculated based on the characteristics of the respective portion of the return line.
  • the blood component separation device further separates the drawn blood into a third blood component in addition to the first blood component and the second blood component.
  • the first blood component may be platelets
  • the second blood component may be red blood cells
  • the third blood component may be plasma.
  • the subject access pressure is determined in real-time.
  • a blood processing device for collecting and exchanging blood components may include a venous-access device and a blood component separation device.
  • the device may utilize the venous access device to draw whole blood from a subject and return unused blood components to the subject.
  • the blood component separation device may separate the drawn whole blood into a first blood component and a second blood component, and send the second blood component to a second blood component storage container.
  • the blood processing device may also have a return line and a draw line.
  • the return line fluidly connects the venous-access device and the blood component separation device and may be used to return the first blood component to the subject.
  • the draw line also fluidly connects the venous-access device and the blood component separation device and may be used to draw whole blood from the subject and into the blood component separation device
  • the blood processing device may also have a first pressure sensor located on the return line and a second pressure sensor located on the draw line.
  • Each of the sensors may be located between the blood component separation device and the venous-access device on their respective lines and may measure a pressure.
  • a pump, connected to the return line, may control the return flow rate based on a subject access pressure determined based on the pressures measured by the sensors.
  • a method of collecting and exchanging blood components using blood processing equipment may include inserting a venous-access device into a subject and withdrawing blood from the subject through a draw line. The method may then separate the withdrawn blood into a first blood component and a second blood component using a blood component separation device. Once the blood is separated into components, the method may extract the second blood component from the blood component separation device and return the first blood component to the subject through a return line.
  • the method may also measure a first pressure and a second pressure using a first sensor and a second sensor, respectively.
  • the first pressure sensor may be located on the return line between the venous-access device and the blood component separation device.
  • the second pressure sensor may be located on the draw line between the venous-access device and the blood component separation device. The method may then control a flow rate based on a subject access pressure determined using the first pressure and the second pressure.
  • FIG. 1A shows a schematic diagram of an apheresis system in accordance with embodiments of the present invention
  • FIG. 1B shows a schematic diagram of an alternative embodiment of an apheresis system in accordance with embodiments of the present invention
  • FIG. 1C shows a schematic diagram of an additional alternative embodiment of an apheresis system in accordance with embodiments of the present invention
  • FIG. 2 schematically shows a disposable system for use with the apheresis system of FIG. 1A , in accordance with one embodiment of the present invention
  • FIG. 3 schematically shows a side view of a blood component separation device for use with the apheresis system of FIG. 1A , in accordance with embodiments of the present invention
  • FIG. 4 shows a flowchart showing the steps of a method of using the apheresis system of FIG. 1A in accordance with one embodiment of the present invention
  • FIG. 5 shows a flowchart showing the steps of a second method of using the apheresis system of FIG. 1A in accordance with an additional embodiment of the present invention.
  • Embodiments of the present invention provide a system and method for performing a blood apheresis procedure. Specific embodiments of the present invention optimize the withdrawal of whole blood from a subject and the return of unharvested or processed blood component to the subject.
  • the method and system may use multiple pressure sensors on the withdraw and/or return line to determine the pressure at the subject access site, and control the flow of fluids within the system based on this pressure. Details of illustrative embodiments are discussed below.
  • an apheresis system 10 withdraws whole blood from a subject through a venous access device 24 using a withdraw pump P 1 .
  • the venous access device 24 can be any number of devices capable of accessing a subject's veins including, but not limited to a phlebotomy needle.
  • a draw/return line 28 As the system 10 withdraws the whole blood from the subject, the blood passes through a draw/return line 28 and enters a blood component separation device 11 , such as a standard Latham type centrifuge.
  • the blood component separation device 11 separates the whole blood into its constituent components (e.g., red blood cells, white blood cell, plasma, and platelets).
  • Latham type centrifuge is mentioned above, other types of separation chambers and devices may be used, such as, without limitation, an integral blow-molded centrifuge bowl, as described in U.S. Pat. Nos. 4,983,156 and 4,943,273, which are hereby incorporated by reference.
  • the system 10 may introduce anticoagulant into the withdrawn whole blood to prevent the blood from coagulating within the lines or within the blood component separation device 11 .
  • the system 10 may include an anticoagulant line 32 fluidly connected to an anticoagulant source 16 (e.g., a bag of anticoagulant) at one end, and the venous-access device 24 (or the draw/return line 28 via a y-connector 30 ) at the other end.
  • An anti-coagulant pump P 3 through which the anticoagulant line 32 passes, may control the flow of anticoagulant within the anti-coagulant line 32 and the amount of anticoagulant introduced into the whole blood.
  • the anticoagulant can be added to the whole blood at any point, it is preferred that the anticoagulant be introduced as close as possible to the venous-access device 24 .
  • the anticoagulant line 32 may also include a bacteria filter F 2 that prevents any bacteria in the anticoagulant source 16 , the anticoagulant, or the anticoagulant line 32 from entering the system 10 and/or the subject. Additionally, the anticoagulant line 32 may include an air detector D 3 that detects the presence of air within the anticoagulant. The presence of air bubbles within any of the system 10 lines can be problematic for the operation the system 10 and may also be harmful to the subject if the air bubbles enter the blood stream.
  • the air detector D 3 may be connected to an interlock that stops the flow within the anticoagulant line 32 in the event that an air bubble is detected (e.g., by stopping the anticoagulant pump P 3 or closing a valve on the anticoagulant line 32 ), thereby preventing the air bubbles from entering the subject.
  • the blood component separation device 11 separates the whole blood into several blood components.
  • the blood component separation device 11 may separate the whole blood into a first, second, third, and, perhaps, fourth blood component. More specifically, the blood component separation device 150 can separate the whole blood into plasma, platelets, red blood cells, and, perhaps, white blood cells.
  • the blood component separation device 11 when a Latham centrifuge is used, the blood component separation device 11 includes a rotatable bowl 12 and stationary input and output ports PT 1 and PT 2 fluidly coupled to the bowl interior by a rotary seal 74 .
  • the draw/return line 28 fluidly connects the venous access devices 24 (e.g., the phlebotomy needle) and the input port PT 1 .
  • the venous access device 24 may be replaced with a whole blood bag (not shown) in case the whole blood is to be first pooled and then supplied. In such embodiments, the draw line 28 will fluidly connect the whole blood bag with the input port PT 1 .
  • the blood component separation device 11 separates the whole blood into its constituent components.
  • centrifugal forces separate the anticoagulated whole blood admitted into the bottom of the bowl into red blood cells (RBC), white blood cells (WBC), platelets and plasma.
  • the number of rotations of the bowl 12 can be selected, for example, within a range of 4,000 to 6,000 rpm, and is typically 4,800 rpm.
  • the blood is separated into different fractions in accordance with the component densities.
  • the higher density component i.e., RBC 60
  • RBC 60 is forced to the outer wall 70 of the bowl 12 while the lower density plasma 66 lies nearer the core 72 .
  • a buffy coat 61 is formed between the plasma 66 and the RBC 60 .
  • the buffy coat 61 is made up of an inner layer of platelets 64 , a transitional layer 68 of platelets and WBC and an outer layer of WBC 62 .
  • the plasma 66 is the component closest to the outlet port from the separation region and is the first fluid component displaced from the bowl 12 via the outlet port PT 2 as additional anticoagulated whole blood enters the bowl 12 through the inlet port PT 1 .
  • the system 10 may also include an optical sensor 21 that may be applied to a shoulder portion of the bowl 12 .
  • the optical sensor 21 monitors each layer of the blood components as they gradually and coaxially advance toward the core 72 from the outer wall 70 of the bowl 12 .
  • the optical sensor 21 may be mounted in a position at which it can detect the buffy coat reaching a particular radius, and the steps of drawing the whole blood from the donor 401 and introducing the whole blood into the bowl 402 may be terminated in response to the detection.
  • the plasma may be removed to a plasma bag 18 through line 37 ( FIG. 1A and FIG. 2 ) or a waste bag (not shown).
  • the plasma may be removed to a plasma reservoir (not shown) located on the draw/return line 28 , or the white blood cells (WBC) may be removed to one or more white blood cell bags 22 via line 35 .
  • Some embodiments of the system 10 may include a weight sensor 33 that measures the amount plasma collected.
  • the platelet bag 20 and the white blood cell bag 22 may include similar weight sensors.
  • the removed plasma may be later reintroduced into the blood component separation device 11 via line 40 and recirculation pump P 2 at an increasing rate to extract and send the platelets to a platelet bag 20 via line 39 .
  • This process is known as surge elutriation.
  • the system 10 may also include a line sensor 14 that can determine the type of fluid (e.g., plasma, platelets, red blood cells etc.) exiting the blood component separation device.
  • the line sensor 14 consists of an LED which emits light through the blood components leaving the bowl 12 and a photo detector which receives the light after it passes through the components. The amount of light received by the photo detector is correlated to the density of the fluid passing through the line. For example, if plasma is exiting the bowl 12 , the line sensor 14 will be able to detect when the plasma exiting the bowl 12 becomes cloudy with platelets (e.g., the fluid existing the bowl 12 is changing from plasma to platelets). The system 10 may then use this information to either stop the removal of blood components from the bowl 12 or redirect the flow by, for example, closing valve V 2 and opening valve V 3 .
  • the system 10 can return the remaining components to the subject.
  • the system may use the draw/return pump P 1 to return the components to the subject via the draw/return line 28 , which, as mentioned above, fluidly connects the blood component separation device 11 and the venous-access device 24 .
  • the system may return the components to the subject via a dedicated return line 27 , FIG. 1B .
  • the dedicated return line 27 may also have a dedicated return pump P 5 that controls the direction, rate, and duration of the fluid flow within the return line.
  • the return line 27 also fluidly connects to the venous-access device 24 , preferably at a point between the return pump P 5 and the venous-access device 24 .
  • the system 10 will also have a dedicated draw line 29 and draw pump P 4 .
  • the system 10 may include an interlock that stops the withdrawal of whole blood from the subject when the system is returning the first blood component to the subject.
  • the system 10 can have a plurality of valves located through-out the system to control the flow of fluid within the system 10 .
  • draw/return line 28 may contain a valve V 1 that allows flow through the lines when open and prevents flow when closed.
  • the lines 35 , 37 and 39 leading to the white blood cell, plasma and platelet bags, respectively may have at least one valve V 2 , V 3 , V 4 , and V 5 (e.g., line 37 has a valve V 2 at the inlet of the plasma bag 18 and a valve V 5 at the outlet of the plasma bag 18 , and line 39 has a valve V 3 at the inlet of the platelet bag 20 ).
  • the inlet to the blood component separation device 11 may have valves (not shown) that either allow or prevent flow to or from the blood component separation device 11 .
  • valves can be either manual or automatic.
  • the valves may be manually operated by the user/technician or can be automatically operated, for example, by a controller, when a particular condition is met (e.g., closing valve V 1 when air is detected in the draw/return line 28 , as discussed below).
  • the draw/return line 28 can also include a number of sensors, filters, and detectors to ensure the safety of the subject and an optimized system operation.
  • the draw/return line 28 may include air detectors D 1 and D 2 to detect the presence (or absence) of air within the line 28 .
  • the air detectors D 1 and D 2 can be connected to an interlock that, when the detectors D 1 and D 2 detect air, stops flow within the draw/return line 28 (e.g., by stopping the draw/return pump P 1 or closing valve V 1 ).
  • the draw line 28 can include a blood filter F 1 that removes any bacteria, contamination, or particulates that may be present in the withdrawn blood or the returning components.
  • the system 10 may also include a system pressure monitor (SPM) M 3 that monitors pressure levels within the system 10 .
  • SPM system pressure monitor
  • the system pressure monitor M 3 can include a sample line 208 ( FIG. 2 ) connected to line 36 (e.g., the line leading from the outlet of the blood component separation device 11 ).
  • embodiments of the present invention include pressure monitors M 1 and M 2 that monitor the pressure within the draw/return line 28 (or dedicated return line 27 and dedicated draw line 29 )
  • the system 10 can use the pressure measurements from pressure sensors M 1 and M 2 to control the flow rate and maintain the pressures within a desired range. Additionally or alternatively, the system 10 may also use this pressure information to obtain an accurate measure of the pressure at the venous access device 24 (e.g., the subject access pressure).
  • the first pressure sensor M 1 may be located on the draw/return line 28 between the venous access device 24 and the blood component separation device 11 .
  • the second pressure sensor M 2 may be located between the venous access device 24 and the first pressure sensor M 1 .
  • the first and second pressure sensors M 1 and M 2 can either be located directly on the draw/return line 28 , or they may be connected to the draw/return line 28 via sample lines 204 and 206 , respectively.
  • the system 10 can then use the pressure measurements from M 1 and M 2 and the characteristics (e.g., length, inner diameter, constitutive materials, etc.) of portion A of the draw/return line 28 (e.g., the portion between the venous access device 24 and the second pressure sensor M 2 ) and portion B of the draw/return line 28 (e.g., the portion between the pressure sensors M 1 and M 2 ) to calculate the subject access pressure.
  • the system 10 may use the known characteristics of the line portions A and B to calculate the resistances of each portion. Because the line characteristics are known prior to the start of processing, the system and or operating technician can calculate the resistances in advance.
  • the system may then calculate, in real-time, the subject access pressure according to the equations described in greater detail below. It is important to note that the equation used by the system is dependent upon whether the system is performing a draw step or a return step.
  • the pressure sensors M 1 and M 2 are described above as being located on the same line (e.g., the draw/return line 28 ), the pressure sensors M 1 and M 2 can be located on different lines. For example, as shown in FIG. 1B , if the system 10 has a dedicated draw line 29 with a draw pump P 4 and a dedicated return line 27 with a return pump P 5 (as discussed above), the pressure sensors M 1 and M 2 may be located on separate lines. For example, pressure sensor M 1 may be located on the return line 27 and pressure sensor M 2 may be located on the draw line 29 . In such embodiments, portion A is located between the venous access device 24 and connector 30 .
  • portion B is dependent on whether the subject access pressure is being determined for a draw step or a return step.
  • portion B shown as B D on FIG. 1B
  • portion B is located between connector 30 and pressure sensor M 2 .
  • portion B is located between connector 30 and pressure sensor M 1 .
  • the above equations may be used when certain conditions are met for correcting P DPM2 for the loss of pressure that occurs in the needle and the needle tubing (e.g., the portion of the tubing located between the needle tip and connector 30 ).
  • the conditions are met when (1) the disposable set is known such that the resistances r and R are known, (2) the needle resistance r or the ration of r/R are not the same in the draw and the return steps, (3) the overall donor line (e.g., the DPM 1 and DPM 2 lines) is full with fluid that may be considered to have a homogenous viscosity, and (4) the relative positions of the venous access device 24 and the pressure sensors M 1 and M 2 are known so as to define P HDPM1 and P HDPM2 .
  • condition (3) is generally met.
  • the fluid at the first pressure sensor e.g., M 1
  • the second pressure sensor e.g., M 2
  • whole blood may be located at the first pressure sensor M 1 and packed red blood cells may be located at the second pressure sensor.
  • the difference in fluid at the pressure sensors may be caused any number of a variety of factors.
  • portions of the line near one of the sensors may contain fluid from a previous process (e.g., the draw process or a prior return process).
  • the difference in fluid can arise as the characteristics of the fluid exiting the separation device change (e.g., as the fluid changes from one blood component to another).
  • there is a period of time e.g., the time required for the fluid to travel between the sensors
  • the first sensor M 1 and the second sensor M 2 are seeing different fluids and, therefore potentially different viscosities.
  • embodiments of the present invention are able to detect and compensate for fluid viscosity changes in the lines.
  • embodiments of the system may compensate for viscosity and fluid changes within the portion of line having resistance R by applying the changes to the portion of the line having resistance r.
  • the system 10 is able to, in real-time, precisely measure the subject access pressure, without knowing the flow rate of the fluid within line 28 or the fluid viscosity.
  • the system 10 may then control the flow rate through draw/return line 28 (or draw line 29 and return line 27 ) based on the pressure measurements from pressure sensors M 1 and M 2 or the calculated subject access pressure. By controlling the flow rate in this manner, the system 10 can maintain the pressure in a desired operating range.
  • the operating range may be determined based on a number of factors including, but not limited to, the size of the venous access device 24 , subject characteristics (age, height, weight, health, etc.), the location of the venous access device 24 (e.g., into which vein it is inserted), cuff pressure, and system characteristics. This allows the system to operate at an optimum flow rate (e.g., the flow rate at which the whole blood is withdrawn and the flow rate at which the components are returned to the subject), without exposing the subject to an increased risk of vein lesions or other complications.
  • an optimum flow rate e.g., the flow rate at which the whole blood is withdrawn and the flow rate at which the components are returned to the subject
  • the system 10 includes a number of lines leading to and from each of the system components. In many instances, multiple lines lead into a single line.
  • the system 10 may include line connectors to connect the lines.
  • the line connectors may be y-site connectors such as connector 30 , which connects the anticoagulant line 32 with the draw/return line 28 , and connector 91 , which connects line 40 coming from the plasma bag 18 and the draw/return line 28 (the outlet of the y-connector is line 41 leading to PT 1 ).
  • the connectors can be T-site connectors such as connector 92 , which connects the lines 37 and 39 with line 36 , and connector 26 which connects the sample line 208 for system pressure monitor M 2 with line 36 .
  • FIG. 4 schematically shows a flowchart depicting a method of using the dual-pressure sensor apheresis system described above.
  • the method first inserts the venous access device 24 into the subject (Step 410 ), and then begins to withdraw whole blood through the draw/return line 28 (or draw line 29 ) (Step 420 ).
  • draw pump P 1 controls the direction, rate, and duration of the flow within the draw/return line 28 .
  • the anticoagulant pump P 3 introduces anticoagulant from the anticoagulant source 16 into the whole blood via the anticoagulant line 32 .
  • the anticoagulant prevents the whole blood from coagulating within the system.
  • the blood component separation device 11 separates the blood into the constituent components (e.g., red blood cells, plasma, platelets, and white blood cells) in the layered orientation described above (Step 430 ).
  • the technician operating the system may then extract one or more of the components (the component extracted is dependent on the purpose of the procedure) (Step 440 ) and return the remaining blood components to the subject (Step 450 ).
  • the method may also measure the pressure within draw/return line 28 (or return line 27 ) at two points using pressure sensors M 1 and M 2 (Steps 460 and 470 ).
  • the system 10 is operating at a safe and optimized flow rate and the system 10 can maintain the current flow rate (Step 482 ). If the first and second pressures are outside of the desired range, the system can adjust the flow rate such that the pressure is within range (Step 484 ). For example, if the pressures are low, the system 10 can increase the flow rate (e.g., by increasing the speed of the draw pump P 1 ) so that that flow rate is optimized. Alternatively, if the pressures are above the desired range, the system 10 can decrease the flow rate (e.g., by decreasing the speed of draw pump P 1 ) so that the flow rate and pressures are safe for the subject.
  • the method of using the dual pressure apheresis may also include several additional, optional steps.
  • the system 10 may use the measured pressures to calculate the subject access pressure (Step 510 ), as described above.
  • the method may then determine whether the subject access pressure is within a desired range (Step 520 ). If the subject access pressure is within range, the method can maintain the flow rate within the draw/return line 28 (or draw line 29 and return line 27 ) (Step 530 ) because it is safe for the subject and optimized.
  • the method can adjust the flow rate such that it is within range (Step 540 ). For example, if the pressures are low, the system 10 can increase the flow rate (e.g., by increasing the speed of the draw pump P 1 ) so that that flow rate is optimized. Alternatively, if the pressures are above the desired range, the system 10 can decrease the flow rate (e.g., by decreasing the speed of draw pump P 1 ) so that the flow rate and pressures are safe for the subject.
  • the draw/return line 28 , draw line 29 , return line 27 , and lines 36 , 37 , and 40 should be compatible with blood and blood components.
  • the platelet bag 20 and the plasma bag 18 should be compatible with platelets and plasma, respectively.
  • the anticoagulant line 32 should be compatible with anticoagulant.

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Abstract

A blood processing device includes a venous-access device, a blood component separation device, a return line, a draw line, a first pressure sensor, a second pressure sensor, and a first pump. The first pressure sensor is located on the return line between the blood component separation device and the venous-access device, and determines a first pressure. The second pressure sensor is located on the draw line between the blood component separation device and the venous-access device, and determines a second pressure. The first pump is connected to at least one of the return line and the draw line and controls a flow rate within the connected line based on a subject access pressure determined based upon the first and second pressures.

Description

PRIORITY
This application claims priority from and is a divisional application of co-pending U.S. patent application Ser. No. 12/102,427, entitled, “System and Method for Optimized Apheresis Draw and Return,” filed on Apr. 14, 2008, and naming Etienne Pagès and Michael Ragusa as inventors, the disclosure of which is incorporated herein, in entirety, by reference.
TECHNICAL FIELD
The present invention relates to systems and methods for blood apheresis and particularly to systems and methods for optimized apheresis draw and return.
BACKGROUND ART
Apheresis is a procedure in which an individual blood component can be separated and collected from whole blood withdrawn from a subject. Typically, whole blood is withdrawn through a needle inserted into the subject's arm and transferred into a cell separator, such as a centrifugal bowl. Once the whole blood is separated into its various components (e.g., plasma, red blood cells, and platelets), one or more of the components can be collected from the centrifugal bowl. The remaining components can be returned to the subject along with a compensation fluid to make up for the volume of the removed component.
While performing apheresis procedures, the technician must balance the procedure time with the safety of the patient. In particular, the technician must perform the procedure as quickly as possible to minimize the procedure time and associated discomfort of the subject, but must always be conscious of the safety of the subject. One such area for safety concern is the pressure at which the whole blood is withdrawn from the subject and the remaining blood components are returned to the subject. The pressure at which the remaining components and potential compensation fluid are returned to the subject is critical to the safety of the subject. If the pressure is too high during the return or too low in during the draw, the subject is at risk for vein lesions.
To control the pressure of the blood withdrawn from and components returned to the subject, current systems attempt to measure a venous pressure. However, current systems typically measure the pressure within the line at a distance away from the access site. This distance creates inaccuracies in the measurement and, as a result, current systems can not accurately measure the venous pressure. As one can imagine, these inaccuracies increase the risk to the patient and, perhaps, force the technician to operate the apheresis system at a non-optimized rate. Despite measuring as close as possible to the venipuncture, current systems do not factor in the loss of pressure that occurs between the point of measure and the tip of the needle,
SUMMARY OF THE INVENTION
Embodiments of the present invention precisely determine donor vein pressure without the need for a sensor to be located within the vein. In some embodiments, pressure may be measured at two points within the line or lines that fluidly connect the needle tip to the apheresis device. The two measurement points (P1 and P2) may be located a distance away from the needle tip within the donor vein. The measurement points may delimit two portions of a line(s) having a known fluid resistance R1 and R2. R may be defined as the change in pressure between the two pressure measurement points divided by a flow rate and may be expressed in mmHg/ml/min. The two portions may include the portion of the line between the needle tip and the first point of measurement and the portion between the first and the second points of measurement. The vein pressure may be determined as a function of the measured pressures and the resistances within the line portions (e.g., Pv=f(P1, P2, R1, R2)) independently from the fluid characteristics and flow rate. Additionally, in some embodiments, Pv, P1 and P2 may be functions of time or of volume processed over time.
In accordance with embodiments of the present invention, a blood processing device for collecting and exchanging blood components includes a venous-access device for drawing whole blood from a subject and returning unused/uncollected blood components and potential compensation fluid to the subject, and a blood component separation device. The blood component separation device (e.g., a centrifuge bowl) separates the drawn whole blood into a first blood component and a second blood component. The blood component separation device may also send the second blood component to a second blood component storage container.
The blood processing device may also have a return line fluidly connecting the venous-access device and the blood component separation device. The system may use the return line to return the first blood component to the subject. The system may also have a first and second pressure sensor located on the return line. The first pressure sensor may be located between the blood component separation device and the venous-access device and may determine a first pressure within the return line. The second pressure sensor may be located between the first pressure sensor and the venous-access device and may determine a second pressure within the return line. A pump connected to the return line may control a return flow rate within the return line based on a subject access pressure determined using the first pressure and the second pressure. The subject access pressure may be determined in real time.
In accordance with other embodiments, the system may also have an anticoagulation line for introducing anticoagulant into the drawn blood near the venous-access device. Additionally, the system may include a valve, located on the return line between the blood component separation device and the venous access device. The valve may stop the flow within the return line. The system may also have an interlock that stops the withdrawal of whole blood from the subject when the system is returning the first blood component to the subject.
In still other embodiments, the subject access pressure may also be based on at least one characteristic of a first portion of the return line and at least one characteristic of a second portion of the return line. The first portion may be between the first and second pressure sensors. The second portion may be between the second pressure sensor and the venous-access device. The characteristics of the first and second portions of the return line may include, but are not limited to, the length, inner diameter, resistance to flow, and materials of construction. The system may also control the return flow rate based on the flow resistances within the first and second portions of the return line. The flow resistances may be calculated based on the line characteristics discussed above.
In accordance with still further embodiments of the present invention the blood component separation device may further separate the drawn blood into a third blood component in addition to the first blood component and the second blood component. The first blood component may be red blood cells, the second blood component may be platelets, and the third blood component may be plasma.
In accordance with other embodiments of the present invention, a method of collecting and exchanging blood components using blood processing equipment includes inserting a venous-access device into a subject, and withdrawing whole blood from the subject. The venous-access device may be fluidly connected to a blood separation device in which the drawn blood is collected. The method then separates the withdrawn blood into a first blood component and a second blood component using the blood component separation device, and extracts the second blood component from the blood component separation device. The system or method may return the remaining components (e.g., the first blood component) to the subject through a return line.
In some embodiments, the method may measure a first pressure within the return line using a first pressure sensor, and a second pressure within the return line using a second pressure sensor. The first and second pressure sensors may be located on the return line. For instance, the first pressure sensor may be located on the return line between the venous-access device and the blood component separation device, and the second pressure sensor may be located on the return line between the venous-access device and the first pressure sensor. The method may then control a return flow rate within the return fluid line based on a subject access pressure that is determined using the first pressure and the second pressure.
In accordance with further embodiments, the subject access pressure may also be determined using at least one characteristic of a first portion of the return line and at least one characteristic of a second portion of the return line. The first portion is between the first and second pressure sensors, and the second portion is between the second pressure sensor and the venous-access device. The characteristics of the line portions can include the length, inner diameter, and materials of construction. The flow rate may also be controlled based on a first flow resistance within the first and/or second portion of the return line. The flow resistances may be calculated based on the characteristics of the respective portion of the return line.
In accordance with still further embodiments of the present invention, the blood component separation device further separates the drawn blood into a third blood component in addition to the first blood component and the second blood component. The first blood component may be platelets, the second blood component may be red blood cells, and the third blood component may be plasma. In some embodiments, the subject access pressure is determined in real-time.
In accordance with other embodiments of the present invention, a blood processing device for collecting and exchanging blood components may include a venous-access device and a blood component separation device. The device may utilize the venous access device to draw whole blood from a subject and return unused blood components to the subject. The blood component separation device may separate the drawn whole blood into a first blood component and a second blood component, and send the second blood component to a second blood component storage container.
The blood processing device may also have a return line and a draw line. The return line fluidly connects the venous-access device and the blood component separation device and may be used to return the first blood component to the subject. The draw line also fluidly connects the venous-access device and the blood component separation device and may be used to draw whole blood from the subject and into the blood component separation device
The blood processing device may also have a first pressure sensor located on the return line and a second pressure sensor located on the draw line. Each of the sensors may be located between the blood component separation device and the venous-access device on their respective lines and may measure a pressure. A pump, connected to the return line, may control the return flow rate based on a subject access pressure determined based on the pressures measured by the sensors.
In accordance with other embodiments, a method of collecting and exchanging blood components using blood processing equipment may include inserting a venous-access device into a subject and withdrawing blood from the subject through a draw line. The method may then separate the withdrawn blood into a first blood component and a second blood component using a blood component separation device. Once the blood is separated into components, the method may extract the second blood component from the blood component separation device and return the first blood component to the subject through a return line.
The method may also measure a first pressure and a second pressure using a first sensor and a second sensor, respectively. The first pressure sensor may be located on the return line between the venous-access device and the blood component separation device. The second pressure sensor may be located on the draw line between the venous-access device and the blood component separation device. The method may then control a flow rate based on a subject access pressure determined using the first pressure and the second pressure.
BRIEF DESCRIPTION OF THE DRAWINGS
The foregoing features of the invention will be more readily understood by reference to the following detailed description, taken with reference to the accompanying drawings, in which:
FIG. 1A shows a schematic diagram of an apheresis system in accordance with embodiments of the present invention;
FIG. 1B shows a schematic diagram of an alternative embodiment of an apheresis system in accordance with embodiments of the present invention;
FIG. 1C shows a schematic diagram of an additional alternative embodiment of an apheresis system in accordance with embodiments of the present invention;
FIG. 2 schematically shows a disposable system for use with the apheresis system of FIG. 1A, in accordance with one embodiment of the present invention;
FIG. 3 schematically shows a side view of a blood component separation device for use with the apheresis system of FIG. 1A, in accordance with embodiments of the present invention;
FIG. 4 shows a flowchart showing the steps of a method of using the apheresis system of FIG. 1A in accordance with one embodiment of the present invention;
FIG. 5 shows a flowchart showing the steps of a second method of using the apheresis system of FIG. 1A in accordance with an additional embodiment of the present invention.
DETAILED DESCRIPTION OF SPECIFIC EMBODIMENTS
Embodiments of the present invention provide a system and method for performing a blood apheresis procedure. Specific embodiments of the present invention optimize the withdrawal of whole blood from a subject and the return of unharvested or processed blood component to the subject. The method and system may use multiple pressure sensors on the withdraw and/or return line to determine the pressure at the subject access site, and control the flow of fluids within the system based on this pressure. Details of illustrative embodiments are discussed below.
As shown in FIGS. 1A and 2, and as mentioned above, an apheresis system 10, in accordance with embodiments of the present invention, withdraws whole blood from a subject through a venous access device 24 using a withdraw pump P1. The venous access device 24 can be any number of devices capable of accessing a subject's veins including, but not limited to a phlebotomy needle. As the system 10 withdraws the whole blood from the subject, the blood passes through a draw/return line 28 and enters a blood component separation device 11, such as a standard Latham type centrifuge. The blood component separation device 11 separates the whole blood into its constituent components (e.g., red blood cells, white blood cell, plasma, and platelets). Although a Latham type centrifuge is mentioned above, other types of separation chambers and devices may be used, such as, without limitation, an integral blow-molded centrifuge bowl, as described in U.S. Pat. Nos. 4,983,156 and 4,943,273, which are hereby incorporated by reference.
As the system 10 withdraws the whole blood from the subject, the system 10 may introduce anticoagulant into the withdrawn whole blood to prevent the blood from coagulating within the lines or within the blood component separation device 11. To that end, the system 10 may include an anticoagulant line 32 fluidly connected to an anticoagulant source 16 (e.g., a bag of anticoagulant) at one end, and the venous-access device 24 (or the draw/return line 28 via a y-connector 30) at the other end. An anti-coagulant pump P3, through which the anticoagulant line 32 passes, may control the flow of anticoagulant within the anti-coagulant line 32 and the amount of anticoagulant introduced into the whole blood. Although the anticoagulant can be added to the whole blood at any point, it is preferred that the anticoagulant be introduced as close as possible to the venous-access device 24.
The anticoagulant line 32 may also include a bacteria filter F2 that prevents any bacteria in the anticoagulant source 16, the anticoagulant, or the anticoagulant line 32 from entering the system 10 and/or the subject. Additionally, the anticoagulant line 32 may include an air detector D3 that detects the presence of air within the anticoagulant. The presence of air bubbles within any of the system 10 lines can be problematic for the operation the system 10 and may also be harmful to the subject if the air bubbles enter the blood stream. Therefore, the air detector D3 may be connected to an interlock that stops the flow within the anticoagulant line 32 in the event that an air bubble is detected (e.g., by stopping the anticoagulant pump P3 or closing a valve on the anticoagulant line 32), thereby preventing the air bubbles from entering the subject.
Once a desired amount of anti-coagulated whole blood is withdrawn from the subject and contained within the blood component separation device 11, the blood component separation device 11 separates the whole blood into several blood components. For example, the blood component separation device 11 may separate the whole blood into a first, second, third, and, perhaps, fourth blood component. More specifically, the blood component separation device 150 can separate the whole blood into plasma, platelets, red blood cells, and, perhaps, white blood cells.
As shown in FIG. 3, when a Latham centrifuge is used, the blood component separation device 11 includes a rotatable bowl 12 and stationary input and output ports PT1 and PT2 fluidly coupled to the bowl interior by a rotary seal 74. The draw/return line 28 fluidly connects the venous access devices 24 (e.g., the phlebotomy needle) and the input port PT1. In some embodiments, the venous access device 24 may be replaced with a whole blood bag (not shown) in case the whole blood is to be first pooled and then supplied. In such embodiments, the draw line 28 will fluidly connect the whole blood bag with the input port PT1.
As mentioned above, the blood component separation device 11 separates the whole blood into its constituent components. In particular, as the bowl 12 rotates, centrifugal forces separate the anticoagulated whole blood admitted into the bottom of the bowl into red blood cells (RBC), white blood cells (WBC), platelets and plasma. The number of rotations of the bowl 12 can be selected, for example, within a range of 4,000 to 6,000 rpm, and is typically 4,800 rpm. The blood is separated into different fractions in accordance with the component densities. The higher density component, i.e., RBC 60, is forced to the outer wall 70 of the bowl 12 while the lower density plasma 66 lies nearer the core 72. A buffy coat 61 is formed between the plasma 66 and the RBC 60. The buffy coat 61 is made up of an inner layer of platelets 64, a transitional layer 68 of platelets and WBC and an outer layer of WBC 62. The plasma 66 is the component closest to the outlet port from the separation region and is the first fluid component displaced from the bowl 12 via the outlet port PT2 as additional anticoagulated whole blood enters the bowl 12 through the inlet port PT1.
The system 10 may also include an optical sensor 21 that may be applied to a shoulder portion of the bowl 12. The optical sensor 21 monitors each layer of the blood components as they gradually and coaxially advance toward the core 72 from the outer wall 70 of the bowl 12. The optical sensor 21 may be mounted in a position at which it can detect the buffy coat reaching a particular radius, and the steps of drawing the whole blood from the donor 401 and introducing the whole blood into the bowl 402 may be terminated in response to the detection.
Once the blood component separation device 11 has separated the blood into the various components, one or more of the components can be removed from the blood component separation device 11. For instance, the plasma may be removed to a plasma bag 18 through line 37 (FIG. 1A and FIG. 2) or a waste bag (not shown). Alternatively, the plasma may be removed to a plasma reservoir (not shown) located on the draw/return line 28, or the white blood cells (WBC) may be removed to one or more white blood cell bags 22 via line 35. Some embodiments of the system 10 may include a weight sensor 33 that measures the amount plasma collected. Although not shown, the platelet bag 20 and the white blood cell bag 22 may include similar weight sensors. The removed plasma may be later reintroduced into the blood component separation device 11 via line 40 and recirculation pump P2 at an increasing rate to extract and send the platelets to a platelet bag 20 via line 39. This process is known as surge elutriation.
In some embodiments, the system 10 may also include a line sensor 14 that can determine the type of fluid (e.g., plasma, platelets, red blood cells etc.) exiting the blood component separation device. In particular, the line sensor 14 consists of an LED which emits light through the blood components leaving the bowl 12 and a photo detector which receives the light after it passes through the components. The amount of light received by the photo detector is correlated to the density of the fluid passing through the line. For example, if plasma is exiting the bowl 12, the line sensor 14 will be able to detect when the plasma exiting the bowl 12 becomes cloudy with platelets (e.g., the fluid existing the bowl 12 is changing from plasma to platelets). The system 10 may then use this information to either stop the removal of blood components from the bowl 12 or redirect the flow by, for example, closing valve V2 and opening valve V3.
Once the system removes the desired components from the blood component separation device 11, the system 10 can return the remaining components to the subject. The system may use the draw/return pump P1 to return the components to the subject via the draw/return line 28, which, as mentioned above, fluidly connects the blood component separation device 11 and the venous-access device 24. Alternatively, if the system 11 is so equipped, the system may return the components to the subject via a dedicated return line 27, FIG. 1B. Like the anticoagulant line 32 and the draw/return line 28, the dedicated return line 27 may also have a dedicated return pump P5 that controls the direction, rate, and duration of the fluid flow within the return line. In such embodiments, the return line 27 also fluidly connects to the venous-access device 24, preferably at a point between the return pump P5 and the venous-access device 24. Additionally, in such embodiments, the system 10 will also have a dedicated draw line 29 and draw pump P4. In some embodiments, the system 10 may include an interlock that stops the withdrawal of whole blood from the subject when the system is returning the first blood component to the subject.
As shown in FIG. 1A and as mentioned briefly above, the system 10 can have a plurality of valves located through-out the system to control the flow of fluid within the system 10. For example, draw/return line 28 may contain a valve V1 that allows flow through the lines when open and prevents flow when closed. Additionally, the lines 35, 37 and 39 leading to the white blood cell, plasma and platelet bags, respectively may have at least one valve V2, V3, V4, and V5 (e.g., line 37 has a valve V2 at the inlet of the plasma bag 18 and a valve V5 at the outlet of the plasma bag 18, and line 39 has a valve V3 at the inlet of the platelet bag 20). Additionally, the inlet to the blood component separation device 11 may have valves (not shown) that either allow or prevent flow to or from the blood component separation device 11. Any of the above mentioned valves can be either manual or automatic. In other words, the valves may be manually operated by the user/technician or can be automatically operated, for example, by a controller, when a particular condition is met (e.g., closing valve V1 when air is detected in the draw/return line 28, as discussed below).
Like the anticoagulant line 32, the draw/return line 28 can also include a number of sensors, filters, and detectors to ensure the safety of the subject and an optimized system operation. In particular, as shown in FIG. 1A, the draw/return line 28 may include air detectors D1 and D2 to detect the presence (or absence) of air within the line 28. The air detectors D1 and D2 can be connected to an interlock that, when the detectors D1 and D2 detect air, stops flow within the draw/return line 28 (e.g., by stopping the draw/return pump P1 or closing valve V1). Additionally, the draw line 28 can include a blood filter F1 that removes any bacteria, contamination, or particulates that may be present in the withdrawn blood or the returning components. The system 10 may also include a system pressure monitor (SPM) M3 that monitors pressure levels within the system 10. Like the first and second pressure monitors M1 and M2, discussed in greater detail below, the system pressure monitor M3 can include a sample line 208 (FIG. 2) connected to line 36 (e.g., the line leading from the outlet of the blood component separation device 11).
As mentioned above, the pressure and flow rate at which the system withdraws blood from the subject and the rate at which the system returns unharvested components to the subject are critical not only to the overall time and efficiency of the procedure, but also the safety of the subject. If the pressure and flow rate are too low, the procedure will take longer than needed, thus increasing the subject's discomfort. However, if the pressure and flow rate are too high, the subject may encounter problems such as vein lesions. To that end, embodiments of the present invention include pressure monitors M1 and M2 that monitor the pressure within the draw/return line 28 (or dedicated return line 27 and dedicated draw line 29)
Unlike prior art systems that monitor the return pressure only at a single point, embodiments of the present invention, as mentioned above, monitor the return pressure at two locations. In some embodiments, the system 10 can use the pressure measurements from pressure sensors M1 and M2 to control the flow rate and maintain the pressures within a desired range. Additionally or alternatively, the system 10 may also use this pressure information to obtain an accurate measure of the pressure at the venous access device 24 (e.g., the subject access pressure).
In embodiments having a shared draw/return line 28, the first pressure sensor M1 may be located on the draw/return line 28 between the venous access device 24 and the blood component separation device 11. The second pressure sensor M2 may be located between the venous access device 24 and the first pressure sensor M1. The first and second pressure sensors M1 and M2 can either be located directly on the draw/return line 28, or they may be connected to the draw/return line 28 via sample lines 204 and 206, respectively. The system 10 can then use the pressure measurements from M1 and M2 and the characteristics (e.g., length, inner diameter, constitutive materials, etc.) of portion A of the draw/return line 28 (e.g., the portion between the venous access device 24 and the second pressure sensor M2) and portion B of the draw/return line 28 (e.g., the portion between the pressure sensors M1 and M2) to calculate the subject access pressure. In particular, the system 10 may use the known characteristics of the line portions A and B to calculate the resistances of each portion. Because the line characteristics are known prior to the start of processing, the system and or operating technician can calculate the resistances in advance.
The system may then calculate, in real-time, the subject access pressure according to the equations described in greater detail below. It is important to note that the equation used by the system is dependent upon whether the system is performing a draw step or a return step.
For example, during a draw step, the system may use the following equation:
P v =P M2 −P HM2+(R A /R B)*((P M2 −PH M2)−(P M1 −PH M1))
Conversely, during the return step, the system may use the following equation:
P v =P M2 −P HM2−(R A /R B)*((P M1 −P HM1)−(P M2 −P HM2))
Where,
    • RA=the resistance to flow in tubing section A (e.g., including the needle, needle line, and draw/return line 28 to sensor M2;
    • RB=the resistance to flow in tubing section B (e.g., including the draw/return line 28 between sensors M1 and M2); and
    • PHM1 and PHM2=the part of PM1 and PM2, respectively, that is associated with the difference in height between the venous access device 24 and the pressure sensors M1 and M2.
Although the pressure sensors M1 and M2 are described above as being located on the same line (e.g., the draw/return line 28), the pressure sensors M1 and M2 can be located on different lines. For example, as shown in FIG. 1B, if the system 10 has a dedicated draw line 29 with a draw pump P4 and a dedicated return line 27 with a return pump P5 (as discussed above), the pressure sensors M1 and M2 may be located on separate lines. For example, pressure sensor M1 may be located on the return line 27 and pressure sensor M2 may be located on the draw line 29. In such embodiments, portion A is located between the venous access device 24 and connector 30. However, the location of portion B is dependent on whether the subject access pressure is being determined for a draw step or a return step. In particular, during a draw step portion B (shown as BD on FIG. 1B) is located between connector 30 and pressure sensor M2. Alternatively, during the return step, portion B (shown as BR on FIG. 1B) is located between connector 30 and pressure sensor M1.
In addition to changing the location of the portions A and B and the location of the pressure sensors M1 and M2, systems having a dedicated return line 27 and dedicated draw line 29 must also utilize different equations to determine the subject access pressure. Additionally, in a similar manner to the systems having only the draw/return line 28, the equations used by the system are dependant upon whether the system is performing a draw step or a return step. For example, during the draw step, the system can determine the subject access pressure according to the following equation:
Pv=P M1 −P HM1 +r D /R D*[(P M1 −P HM1)−(P M2 −P HM2)]
where
    • R is the resistance to flow of the donor line (e.g., portion BD),
    • r is the resistance to flow of the needle and the needle tubing (e.g., portion A), and
    • PHM2 and PHM1 respectively stand for the part of PM2 and PM1 that is associated with the difference in height between the vein puncture and the pressure sensors.
Conversely, during the return step, the system can determine the subject access pressure according to the following equation:
Pv=P M2 −P HM2 −r R /R R*[(P M1 −P HM1)−(P M2 −P HM2)]
where
    • R is the resistance to flow of the donor line (e.g., portion BR),
    • r is the resistance to flow of the needle and the needle tubing (e.g., portion A), and
    • PHM2 and PHM1 respectively stand for the part of PM2 and PM1 that is associated with the difference in height between the vein puncture and the pressure sensors.
It is important to note that the above equations may be used when certain conditions are met for correcting PDPM2 for the loss of pressure that occurs in the needle and the needle tubing (e.g., the portion of the tubing located between the needle tip and connector 30). In particular, the conditions are met when (1) the disposable set is known such that the resistances r and R are known, (2) the needle resistance r or the ration of r/R are not the same in the draw and the return steps, (3) the overall donor line (e.g., the DPM1 and DPM2 lines) is full with fluid that may be considered to have a homogenous viscosity, and (4) the relative positions of the venous access device 24 and the pressure sensors M1 and M2 are known so as to define PHDPM1 and PHDPM2.
It is important to note that during the draw process, there is generally no need to account for any differences in fluid viscosities. In particular, this is because the nature of processed fluid during draw is always whole blood or anticoagulated whole blood. Therefore, condition (3), mentioned above, is generally met. However, during the return process, the fluid at the first pressure sensor (e.g., M1) may be different from that at the second pressure sensor (e.g., M2). For example, whole blood may be located at the first pressure sensor M1 and packed red blood cells may be located at the second pressure sensor. The difference in fluid at the pressure sensors may be caused any number of a variety of factors. For example, portions of the line near one of the sensors may contain fluid from a previous process (e.g., the draw process or a prior return process). Additionally or alternatively, the difference in fluid can arise as the characteristics of the fluid exiting the separation device change (e.g., as the fluid changes from one blood component to another). In either scenario, there is a period of time (e.g., the time required for the fluid to travel between the sensors) that the first sensor M1 and the second sensor M2 are seeing different fluids and, therefore potentially different viscosities.
In part because of the ability for real time determination of pressures, embodiments of the present invention are able to detect and compensate for fluid viscosity changes in the lines. For example, embodiments of the system may compensate for viscosity and fluid changes within the portion of line having resistance R by applying the changes to the portion of the line having resistance r. Under a mathematically simplified form, when the condition (3) is not met, the equation may become:
Pv(t)=P M2(t)−P HM2 −r R /R R*[(P M1(t−Δt)−P HM1)−(P M2(t−Δt)−P HM2)]/Flow(t−Δt)×Flow(t)
where
Δt can be broadly defined as the time needed for the fluid of changed viscosity to travel from the portion of line of resistance R to that of resistance r.
Accordingly, the system 10 is able to, in real-time, precisely measure the subject access pressure, without knowing the flow rate of the fluid within line 28 or the fluid viscosity. The system 10 may then control the flow rate through draw/return line 28 (or draw line 29 and return line 27) based on the pressure measurements from pressure sensors M1 and M2 or the calculated subject access pressure. By controlling the flow rate in this manner, the system 10 can maintain the pressure in a desired operating range. The operating range may be determined based on a number of factors including, but not limited to, the size of the venous access device 24, subject characteristics (age, height, weight, health, etc.), the location of the venous access device 24 (e.g., into which vein it is inserted), cuff pressure, and system characteristics. This allows the system to operate at an optimum flow rate (e.g., the flow rate at which the whole blood is withdrawn and the flow rate at which the components are returned to the subject), without exposing the subject to an increased risk of vein lesions or other complications.
As shown in FIGS. 1A-C and 2 and as discussed above, the system 10 includes a number of lines leading to and from each of the system components. In many instances, multiple lines lead into a single line. In such cases, the system 10 may include line connectors to connect the lines. The line connectors may be y-site connectors such as connector 30, which connects the anticoagulant line 32 with the draw/return line 28, and connector 91, which connects line 40 coming from the plasma bag 18 and the draw/return line 28 (the outlet of the y-connector is line 41 leading to PT1). Alternatively, the connectors can be T-site connectors such as connector 92, which connects the lines 37 and 39 with line 36, and connector 26 which connects the sample line 208 for system pressure monitor M2 with line 36.
FIG. 4 schematically shows a flowchart depicting a method of using the dual-pressure sensor apheresis system described above. In particular, the method first inserts the venous access device 24 into the subject (Step 410), and then begins to withdraw whole blood through the draw/return line 28 (or draw line 29) (Step 420). As mentioned above, draw pump P1 controls the direction, rate, and duration of the flow within the draw/return line 28. As the system 10 withdraws the whole blood from the subject, the anticoagulant pump P3 introduces anticoagulant from the anticoagulant source 16 into the whole blood via the anticoagulant line 32. As described above, the anticoagulant prevents the whole blood from coagulating within the system.
Once the anticoagulated whole blood reaches the blood component separation device 11, the blood component separation device 11 separates the blood into the constituent components (e.g., red blood cells, plasma, platelets, and white blood cells) in the layered orientation described above (Step 430). The technician operating the system may then extract one or more of the components (the component extracted is dependent on the purpose of the procedure) (Step 440) and return the remaining blood components to the subject (Step 450). As the method 10 returns the components to the subject, the method may also measure the pressure within draw/return line 28 (or return line 27) at two points using pressure sensors M1 and M2 (Steps 460 and 470). If the first and second pressures are within the appropriate range (Step 480), the system 10 is operating at a safe and optimized flow rate and the system 10 can maintain the current flow rate (Step 482). If the first and second pressures are outside of the desired range, the system can adjust the flow rate such that the pressure is within range (Step 484). For example, if the pressures are low, the system 10 can increase the flow rate (e.g., by increasing the speed of the draw pump P1) so that that flow rate is optimized. Alternatively, if the pressures are above the desired range, the system 10 can decrease the flow rate (e.g., by decreasing the speed of draw pump P1) so that the flow rate and pressures are safe for the subject.
In accordance with other embodiments, and as shown in FIG. 5, the method of using the dual pressure apheresis may also include several additional, optional steps. In particular, after measuring the first pressure (Step 460) and the second pressure (Step 470), the system 10 may use the measured pressures to calculate the subject access pressure (Step 510), as described above. The method may then determine whether the subject access pressure is within a desired range (Step 520). If the subject access pressure is within range, the method can maintain the flow rate within the draw/return line 28 (or draw line 29 and return line 27) (Step 530) because it is safe for the subject and optimized. If the subject access pressure is outside of the range, the method can adjust the flow rate such that it is within range (Step 540). For example, if the pressures are low, the system 10 can increase the flow rate (e.g., by increasing the speed of the draw pump P1) so that that flow rate is optimized. Alternatively, if the pressures are above the desired range, the system 10 can decrease the flow rate (e.g., by decreasing the speed of draw pump P1) so that the flow rate and pressures are safe for the subject.
It should be noted that all of the components of the system should be made of suitable materials that are compatible with the substance with which they are in contact. For example, the draw/return line 28, draw line 29, return line 27, and lines 36, 37, and 40 should be compatible with blood and blood components. Additionally, the platelet bag 20 and the plasma bag 18 should be compatible with platelets and plasma, respectively. Likewise, the anticoagulant line 32 should be compatible with anticoagulant.
Although the above discussion discloses various exemplary embodiments of the invention, it should be apparent that those skilled in the art can make various modifications that will achieve some of the advantages of the invention without departing from the true scope of the invention.

Claims (14)

We claim:
1. A blood processing device for collecting and exchanging blood components, the blood processing device comprising:
a venous-access device for drawing whole blood from a subject and returning unused blood components to the subject;
a blood component separation device for separating the drawn whole blood into a first blood component and a second blood component, the blood component separation device configured to send the second blood component to a second blood component storage container;
a draw/return line fluidly connecting the venous-access device and the blood component separation device for drawing whole blood from a subject and returning the first blood component to the subject;
a first pressure sensor located on the draw/return line between the blood component separation device and the venous-access device for determining a first pressure within the draw/return line;
a second pressure sensor located on the draw/return line between the first pressure sensor and the venous-access device for determining a second pressure within the draw/return line; and
a pump connected to the draw/return line for controlling a flow rate within the draw/return line, the pump controlling the flow rate based on a subject access pressure determined based on the first pressure and the second pressure.
2. A blood processing system according to claim 1, wherein the venous access device may also be used for returning compensation fluid to the subject.
3. A blood processing system according to claim 1, wherein the blood component separation device is a centrifuge bowl.
4. A blood processing system according to claim 1, further comprising an anticoagulation line for introducing anticoagulant into the drawn blood near the venous-access device.
5. A blood processing system according to claim 1 further including a valve located on the draw/return line between the blood component separation device and the venous-access device, the valve stopping the flow within the draw/return line.
6. A blood processing device according to claim 1, wherein the subject access pressure is further based on at least one characteristic of a first portion of the draw/return line and at least one characteristic of a second portion of the draw/return line, wherein the first portion is between the second pressure sensor and the venous-access device and the second portion is between the first and second pressure sensors.
7. A blood processing device according to claim 6, wherein the at least one characteristic of the first portion of the draw/return line and the at least one characteristic of the second portion of the draw/return line are selected from the group consisting of length, inner diameter, and materials of construction.
8. A blood processing device according to claim 6, wherein the flow rate is also controlled based on a first flow resistance within the first portion of the draw/return line, the first flow resistance calculated based on the at least one characteristic of the first portion of the draw/return line.
9. A blood processing device according to claim 8, wherein the flow rate is further controlled based on a second flow resistance within the second portion of the draw/return line, the second flow resistance calculated based on the at least one characteristic of the second portion of the draw/return line.
10. A blood processing device according to claim 1, wherein the blood component separation device further separates the drawn blood into a third blood component in addition to the first blood component and the second blood component.
11. A blood processing device according to claim 10, wherein the first blood component is red blood cells, the second blood component is platelets, and the third blood component is plasma.
12. A blood processing device according to claim 1, wherein the subject access pressure is determined in real-time.
13. A blood processing device according to claim 1, wherein the flow rate is at least one of a draw flow rate and a return flow rate.
14. A blood processing device according to claim 1, wherein the first and second pressure sensors are located between the pump and the venous access device.
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9486590B2 (en) 2014-09-29 2016-11-08 Fenwal, Inc. Automatic purging of air from a fluid processing system
US9498567B2 (en) 2014-09-29 2016-11-22 Fenwal, Inc. Systems and methods for controlling the return phase of a blood separation procedure
US10220132B2 (en) 2014-12-19 2019-03-05 Fenwal, Inc. Biological fluid flow control apparatus and method
US20210205734A1 (en) * 2019-06-06 2021-07-08 Pneumatic Scale Corporation Centrifuge System for Separating Cells in Suspension
US12078630B2 (en) 2018-01-05 2024-09-03 Path Ex, Inc. Device for the capture and removal of disease material from fluids

Families Citing this family (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8628489B2 (en) * 2008-04-14 2014-01-14 Haemonetics Corporation Three-line apheresis system and method
US8702637B2 (en) 2008-04-14 2014-04-22 Haemonetics Corporation System and method for optimized apheresis draw and return
US9164079B2 (en) * 2011-03-17 2015-10-20 Greyledge Technologies Llc Systems for autologous biological therapeutics
JP2014519878A (en) 2011-05-06 2014-08-21 ヘモネティクス・コーポレーション System and method for automatic separation of whole blood
US11386993B2 (en) 2011-05-18 2022-07-12 Fenwal, Inc. Plasma collection with remote programming
US9283316B2 (en) * 2011-05-27 2016-03-15 Grifols, S.A. Priming anticoagulant alignment for blood extraction
US9327296B2 (en) 2012-01-27 2016-05-03 Fenwal, Inc. Fluid separation chambers for fluid processing systems
CN104812421B (en) 2012-08-15 2017-06-06 旋风医疗科技股份有限公司 For the system and method for the Blood calldack from absorbable surgical material
AU2013337284B2 (en) 2012-11-05 2018-03-08 Haemonetics Corporation Continuous flow separation chamber
US8803090B2 (en) 2012-11-09 2014-08-12 Fenwal, Inc. Citrate detector for blood processing system
CN103055365B (en) * 2013-01-22 2016-03-02 欧阳锡林 The blood processing system of autologous storage blood
JP6487339B2 (en) 2013-01-23 2019-03-20 シー・アール・バード・インコーポレーテッドC R Bard Incorporated Low profile access port
US11464960B2 (en) 2013-01-23 2022-10-11 C. R. Bard, Inc. Low-profile single and dual vascular access device
US11420033B2 (en) 2013-01-23 2022-08-23 C. R. Bard, Inc. Low-profile single and dual vascular access device
JP6257406B2 (en) * 2014-03-25 2018-01-10 テルモ株式会社 Red blood cell phlebotomy tool
CN104667362A (en) * 2015-03-24 2015-06-03 傅敏 Full-automatic whole blood collection separator and matched disposable collecting-separating device
EP3124063B1 (en) 2015-07-29 2019-04-10 Fenwal, Inc. Five-port blood separation chamber and methods of using the same
CN105816928A (en) * 2016-05-27 2016-08-03 四川南格尔生物科技有限公司 Blood composition acquisition device and method
US11865243B2 (en) 2016-08-30 2024-01-09 Nxstage Medical, Inc. Parameter monitoring in medical treatment systems
US10758652B2 (en) 2017-05-30 2020-09-01 Haemonetics Corporation System and method for collecting plasma
US10792416B2 (en) 2017-05-30 2020-10-06 Haemonetics Corporation System and method for collecting plasma
USD870264S1 (en) 2017-09-06 2019-12-17 C. R. Bard, Inc. Implantable apheresis port
EP3765044A4 (en) 2018-03-12 2021-12-08 Medeor Therapeutics, Inc. Methods for treating non-cancerous disorders using hematopoietic cells
US11065376B2 (en) 2018-03-26 2021-07-20 Haemonetics Corporation Plasmapheresis centrifuge bowl
US10881692B2 (en) 2018-04-05 2021-01-05 Medeor Therapeutics, Inc. Compositions for establishing mixed chimerism and methods of manufacture thereof
US10842821B2 (en) 2018-04-05 2020-11-24 Medeor Therapeutics, Inc. Cellular compositions derived from prior organ donors and methods of manufacture and use thereof
HUE056564T2 (en) 2018-05-21 2022-02-28 Fenwal Inc Systems for optimization of plasma collection volumes
US11412967B2 (en) 2018-05-21 2022-08-16 Fenwal, Inc. Systems and methods for plasma collection
US12033750B2 (en) 2018-05-21 2024-07-09 Fenwal, Inc. Plasma collection
US11813376B2 (en) 2018-09-18 2023-11-14 Medeor Therapeutics, Inc. Cellular compositions derived from deceased donors to promote graft tolerance and manufacture and uses thereof
US11435350B2 (en) 2018-09-18 2022-09-06 Medeor Therapeutics, Inc. Methods of analysis of blood from deceased donors
CA3145478A1 (en) 2019-08-01 2021-02-04 Greg FLEXMAN Method for controlling the amount of anticoagulant present in collected plasma after apheresis

Citations (173)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1025059A (en) 1911-02-24 1912-04-30 Joseph Eleuterio Hatton Process of centrifugal separation.
US1611725A (en) 1925-05-07 1926-12-21 Maskin Och Brobyggnads Ab Clarifier
US2087778A (en) 1936-01-07 1937-07-20 Kone Ja Silta O Y Maskin Och B Centrifugal machine for filtering purposes
US2661150A (en) 1947-12-17 1953-12-01 Jr William G Abbott Centrifuge
US2750107A (en) 1952-10-02 1956-06-12 Glacier Co Ltd Centrifugal oil cleaner, including a cylindrical filter
US2792172A (en) 1953-03-03 1957-05-14 Glacier Co Ltd Centrifugal filters
US3096283A (en) 1959-06-24 1963-07-02 Becton Dickinson Co Container for blood and machine for separating precipitates from liquid blood constituents
US3145713A (en) 1963-09-12 1964-08-25 Protein Foundation Inc Method and apparatus for processing blood
US3239136A (en) 1962-05-07 1966-03-08 George N Hein Centrifuge and centrifuge head for separating constituents of a liquid and a liner therefor
US3244362A (en) 1959-06-24 1966-04-05 George N Hein Centrifuging apparatus and fractionating system
US3409213A (en) 1967-01-23 1968-11-05 500 Inc Rotary seal and centrifuge incorporation
US3456875A (en) 1966-08-18 1969-07-22 George N Hein Air driven centrifuge
US3489145A (en) 1966-08-08 1970-01-13 Surgeon General Of The Public Method and apparatus for continuous separation of blood in vivo
US3565330A (en) 1968-07-11 1971-02-23 Cryogenic Technology Inc Rotary seal and centrifuge incorporating same
US3655058A (en) 1970-07-13 1972-04-11 Richard A Novak Filtration apparatus
US3737096A (en) 1971-12-23 1973-06-05 Ibm Blood processing control apparatus
US3774840A (en) 1972-01-17 1973-11-27 Environs Dev Inc Centrifugal separator
FR2258898A1 (en) 1974-01-29 1975-08-22 Heraeus Christ Gmbh
US4007871A (en) 1975-11-13 1977-02-15 International Business Machines Corporation Centrifuge fluid container
US4010894A (en) 1975-11-21 1977-03-08 International Business Machines Corporation Centrifuge fluid container
US4014497A (en) 1975-04-22 1977-03-29 Escher Wyss Limited Vertical centrifuge
US4040965A (en) 1975-07-03 1977-08-09 Firma Supraton Aurer & Zucker Ohg Rotary filter separator
US4056224A (en) 1975-03-27 1977-11-01 Baxter Travenol Laboratories, Inc. Flow system for centrifugal liquid processing apparatus
US4082217A (en) 1973-08-27 1978-04-04 Separex Sa Centrifuge apparatus
US4086924A (en) 1976-10-06 1978-05-02 Haemonetics Corporation Plasmapheresis apparatus
US4140268A (en) 1977-03-15 1979-02-20 Haemo-Transfer S.A. Centrifugating device for biological liquids, having a rotatable container, and supporting bracket therefor
US4142670A (en) 1978-01-27 1979-03-06 Beckman Instruments, Inc. Chylomicron rotor
US4151844A (en) 1977-11-11 1979-05-01 Baxter Travenol Laboratories, Inc. Method and apparatus for separating whole blood into its components and for automatically collecting one component
SU660718A1 (en) 1977-04-25 1979-05-05 Специальное Конструкторское Бюро Биофизической Аппаратуры Robot for separating blood and flushing the heavier fraction
US4197847A (en) 1977-03-31 1980-04-15 Isaac Djerassi Method and apparatus for collecting transfusable granulocytes
SU762982A1 (en) 1978-09-22 1980-09-15 Sp K B Biofizicheskoj Apparatu Rotor for blood separation and washing heavy fraction
GB2047110A (en) 1979-03-28 1980-11-26 Hoegman Claes Folke Separating blood components
US4285464A (en) 1979-01-22 1981-08-25 Haemonetics Corporation Apparatus for separation of blood into components thereof
US4300717A (en) 1979-04-02 1981-11-17 Haemonetics Corporation Rotary centrifuge seal
US4303193A (en) 1979-01-22 1981-12-01 Haemonetics Corporation Apparatus for separating blood into components thereof
US4321921A (en) 1978-08-17 1982-03-30 Solco Basel Ag Apparatus for sucking blood out of body cavities
US4387848A (en) 1977-10-03 1983-06-14 International Business Machines Corporation Centrifuge assembly
US4425114A (en) 1981-04-23 1984-01-10 Haemonetics Corporation Blood donation unit
US4430072A (en) 1977-06-03 1984-02-07 International Business Machines Corporation Centrifuge assembly
US4447221A (en) 1982-06-15 1984-05-08 International Business Machines Corporation Continuous flow centrifuge assembly
US4457747A (en) 1980-05-30 1984-07-03 Tu Ho C Exchange transfusion machine
US4464167A (en) 1981-09-03 1984-08-07 Haemonetics Corporation Pheresis apparatus
US4466888A (en) 1980-05-20 1984-08-21 Haemonetics Corporation Suction liquid collection assembly and flexible collecting bag therefor
US4482342A (en) 1982-06-17 1984-11-13 Haemonetics Corporation Blood processing system for cell washing
EP0128683A2 (en) 1983-05-26 1984-12-19 BAXTER INTERNATIONAL INC. (a Delaware corporation) Single needle blood fractionation system having adjustable recirculation through filter
US4490135A (en) 1982-09-24 1984-12-25 Extracorporeal Medical Specialties, Inc. Single needle alternating blood flow system
SU1146098A1 (en) 1983-05-11 1985-03-23 Специальное Конструкторское Бюро Биофизической Аппаратуры Rotor for separating blood and washing heavy fractions
US4530691A (en) 1983-12-13 1985-07-23 Baxter Travenol Laboratories, Inc. Centrifuge with movable mandrel
US4534863A (en) 1984-05-22 1985-08-13 Schleicher & Schuell, Inc. Centrifugal filtering device and filter unit therefor
EP0171749A1 (en) 1984-08-07 1986-02-19 TERUMO KABUSHIKI KAISHA trading as TERUMO CORPORATION Apparatus for separating blood plasma, and apparatus therefor
EP0208061A1 (en) 1985-05-14 1987-01-14 Biotest Pharma GmbH Method and device for obtaining blood plasma
US4643714A (en) 1985-08-05 1987-02-17 Cobe Laboratories, Inc. Single needle apparatus
US4647279A (en) 1985-10-18 1987-03-03 Cobe Laboratories, Inc. Centrifugal separator
US4655742A (en) * 1983-07-13 1987-04-07 Rhone-Poulenc S.A. Process/apparatus for the withdrawal/return of body fluids
US4680025A (en) 1982-08-24 1987-07-14 Baxter Travenol Laboratories, Inc. Blood component collection systems and methods
US4684361A (en) 1985-10-11 1987-08-04 Cardiovascular Systems, Inc. Centrifuge
US4687580A (en) * 1982-01-11 1987-08-18 Rhone-Poulenc S.A. Membrane apparatus/process adapted for plasmapheresis
US4692136A (en) 1985-10-11 1987-09-08 Cardiovascular Systems Inc. Centrifuge
US4708712A (en) 1986-03-28 1987-11-24 Cobe Laboratories, Inc. Continuous-loop centrifugal separator
US4713176A (en) 1985-04-12 1987-12-15 Hemascience Laboratories, Inc. Plasmapheresis system and method
EP0257755A1 (en) 1986-07-22 1988-03-02 Haemonetics Corporation Centrifuge bowl or rotor for plasmapheresis
US4734089A (en) 1976-05-14 1988-03-29 Baxter Travenol Laboratories, Inc. Centrifugal blood processing system
US4740313A (en) 1985-08-12 1988-04-26 Baxter Travenol Laboratories, Inc. Method of filtering using a rotating and oscillating spinner
US4740202A (en) 1984-10-12 1988-04-26 Haemonetics Corporation Suction collection device
US4755300A (en) 1985-12-23 1988-07-05 Haemonetics Corporation Couette membrane filtration apparatus for separating suspended components in a fluid medium using high shear
US4767396A (en) 1987-03-03 1988-08-30 Haemonetics Corporation Method and apparatus for processing biological fluids
US4795419A (en) 1985-10-11 1989-01-03 Kardiothor, Inc. Centrifuge
US4795448A (en) 1986-08-08 1989-01-03 Haemonetics Corporation Suction collection system
US4806252A (en) 1987-01-30 1989-02-21 Baxter International Inc. Plasma collection set and method
US4806247A (en) 1985-04-12 1989-02-21 Baxter International Inc. Plasmapheresis system and method
US4808307A (en) 1985-12-23 1989-02-28 Haemonetics Corporation Couette membrane filtration apparatus for separating suspended components in a fluid medium using high shear
US4850995A (en) 1987-08-19 1989-07-25 Cobe Laboratories, Inc. Centrifugal separation of blood
US4869812A (en) 1985-08-12 1989-09-26 Baxter International Inc. Disposable diagnostic plasma filter dispenser
US4871462A (en) 1985-12-23 1989-10-03 Haemonetics Corporation Enhanced separation of blood components
US4876013A (en) 1983-12-20 1989-10-24 Membrex Incorporated Small volume rotary filter
US4889524A (en) 1987-09-04 1989-12-26 Haemonetics Corporation Portable centrifuge apparatus
US4911833A (en) 1984-08-24 1990-03-27 William F. McLaughlin Closed hemapheresis system and method
US4934995A (en) 1977-08-12 1990-06-19 Baxter International Inc. Blood component centrifuge having collapsible inner liner
US4940543A (en) 1987-01-30 1990-07-10 Baxter International Inc. Plasma collection set
US4943273A (en) 1986-07-22 1990-07-24 Haemonetics Corporation Disposable centrifuge bowl for blood processing
US4968295A (en) 1986-09-22 1990-11-06 Fresenius Ag Method of separating the constituents of the blood
US4983158A (en) 1986-07-22 1991-01-08 Haemonetics Corporation Plasmapheresis centrifuge bowl
US4983156A (en) 1989-07-03 1991-01-08 Benjamin Knelson Centrifugal separator
US4985153A (en) 1988-06-23 1991-01-15 Asahi Medical Co., Ltd. Method for separating blood into blood components, and blood components separator unit
US4994188A (en) 1988-02-05 1991-02-19 Baxter International Inc. Adaptive filtrate flow control system using controlled reduction in filter efficiency
US5039401A (en) 1990-05-16 1991-08-13 Eastman Kodak Company Blood collection and centrifugal separation device including a valve
US5045048A (en) 1990-03-29 1991-09-03 Haemonetics Corporation Rotary centrifuge bowl and seal for blood processing
US5098373A (en) 1989-07-19 1992-03-24 Fresenius Ag Process for controlling blood pumps in the extra-corporeal circuit of a single needle arrangement and apparatus thereof
US5098372A (en) 1986-04-24 1992-03-24 Stafilum Ab Methods and machine based on blood separation by filtration for plasma exchange treatment, plasma donation and cytapheresis such as platelet apheresis
US5100564A (en) 1990-11-06 1992-03-31 Pall Corporation Blood collection and processing system
US5100372A (en) 1990-03-02 1992-03-31 Haemonetics Corporation Core for blood processing apparatus
US5112298A (en) 1990-06-25 1992-05-12 Baxter International Inc. Apheresis method and device
US5114396A (en) 1987-09-15 1992-05-19 Omega Medicinteknik Ab Method of washing blood cells and container assembly thereof
US5135667A (en) 1990-06-14 1992-08-04 Baxter International Inc. Method and apparatus for administration of anticoagulant to red cell suspension output of a blood separator
US5141486A (en) 1990-11-05 1992-08-25 Cobe Laboratories, Inc. Washing cells
US5154716A (en) 1990-11-06 1992-10-13 Miles Inc. Bottom blood bag separation system
US5174894A (en) 1987-06-25 1992-12-29 Terumo Kabushiki Kaisha Blood component separation apparatus
US5194145A (en) 1984-03-21 1993-03-16 William F. McLaughlin Method and apparatus for separation of matter from suspension
US5217427A (en) 1977-08-12 1993-06-08 Baxter International Inc. Centrifuge assembly
US5217426A (en) 1977-08-12 1993-06-08 Baxter International Inc. Combination disposable plastic blood receiving container and blood component centrifuge
US5234403A (en) 1990-05-25 1993-08-10 Sumitomo Bakelite Co., Ltd. Blood collecting apparatus
US5254248A (en) 1990-06-28 1993-10-19 Terumo Kabushiki Kaisha Blood plasma separating apparatus
US5273517A (en) 1991-07-09 1993-12-28 Haemonetics Corporation Blood processing method and apparatus with disposable cassette
US5277701A (en) 1991-11-15 1994-01-11 Regents Of The University Of Minnesota Treatment of aluimmunization and refractoriness to platelet transfusion by protein A column therapy
EP0578086A1 (en) 1992-06-30 1994-01-12 Terumo Kabushiki Kaisha Apparatus and method for transferring separated components in liquid
US5298171A (en) 1991-08-09 1994-03-29 Fresenius Ag Method and apparatus for separation of blood into its components
US5298016A (en) 1992-03-02 1994-03-29 Advanced Haemotechnologies Apparatus for separating plasma and other wastes from blood
US5300060A (en) 1989-06-12 1994-04-05 Miles Inc. Blood bag system for separation and isolation of neocytes and gerocytes
US5316540A (en) 1993-01-13 1994-05-31 Cobe Laboratories Apparatus and method for separating microscopic units in a substantially continuous density gradient solution
US5318512A (en) 1991-09-06 1994-06-07 Fresenius Ag Blood separation device
US5318511A (en) 1991-02-06 1994-06-07 Hospal Industrie Method and apparatus for controlling the circulation of blood in a single needle circuit
EP0619145A2 (en) 1993-04-05 1994-10-12 Electromedics, Inc. Rotary seal for centrifuge
US5368555A (en) 1992-12-29 1994-11-29 Hepatix, Inc. Organ support system
US5387187A (en) 1992-12-01 1995-02-07 Haemonetics Corporation Red cell apheresis method
US5387174A (en) 1993-01-29 1995-02-07 Elp Rochat Centrifugal separator with disposable bowl assembly
US5386734A (en) 1992-08-21 1995-02-07 Fresenius Ag Centrifuge system for the separation of blood into its components
US5403272A (en) 1992-05-29 1995-04-04 Baxter International Inc. Apparatus and methods for generating leukocyte free platelet concentrate
US5405308A (en) 1992-10-13 1995-04-11 Haemonetics Corporation Disposable centrifuge rotor and core for blood processing
EP0654277A1 (en) 1993-10-21 1995-05-24 Cobe Laboratories, Inc. Blood component collection system with optimizer
US5431814A (en) 1993-10-22 1995-07-11 Jorgensen; Glen Centrifugal filter apparatus and method
EP0664159A1 (en) 1994-01-21 1995-07-26 Haemonetics Corporation Plural collector centrifuge bowl for blood processing
US5437598A (en) 1994-01-21 1995-08-01 Cobe Laboratories, Inc. Automation of plasma sequestration
US5437624A (en) 1993-08-23 1995-08-01 Cobe Laboratories, Inc. Single needle recirculation system for harvesting blood components
US5462667A (en) 1990-10-05 1995-10-31 Pall Corporation Filter for liquor filtration
US5470483A (en) 1993-03-22 1995-11-28 Hospal Industrie Device and method for controlling the balance of fluids in an extracorporeal blood circuit
US5484396A (en) 1988-11-17 1996-01-16 Naficy; Sadeque S. Method and device for treatment of HIV infections and AIDS
US5494592A (en) 1993-04-27 1996-02-27 Haemonetics Corporation Apheresis apparatus and method
US5543062A (en) 1992-10-07 1996-08-06 Asahi Medical Co., Ltd. Leukocyte-removing filter device and system and method of using thereof
US5551941A (en) 1993-10-14 1996-09-03 E. I. Du Pont De Nemours And Company Automatic sample container handling centrifuge and a rotor for use therein
US5585007A (en) 1994-12-07 1996-12-17 Plasmaseal Corporation Plasma concentrate and tissue sealant methods and apparatuses for making concentrated plasma and/or tissue sealant
US5643193A (en) * 1995-12-13 1997-07-01 Haemonetics Corporation Apparatus for collection washing and reinfusion of shed blood
US5651766A (en) 1995-06-07 1997-07-29 Transfusion Technologies Corporation Blood collection and separation system
US5656163A (en) 1987-01-30 1997-08-12 Baxter International Inc. Chamber for use in a rotating field to separate blood components
US5665061A (en) 1992-08-11 1997-09-09 Cobe Laboratories, Inc. Biological/pharmaceutical method and apparatus for collecting and mixing fluids
EP0799645A1 (en) 1996-04-03 1997-10-08 Haemonetics Corporation Centrifuge bowl for blood processing
US5733545A (en) 1995-03-03 1998-03-31 Quantic Biomedical Partners Platelet glue wound sealant
US5733253A (en) 1994-10-13 1998-03-31 Transfusion Technologies Corporation Fluid separation system
US5733446A (en) 1994-12-02 1998-03-31 Bristol-Myers Squibb Company Centrifuge with annular filter
US5762791A (en) 1995-08-09 1998-06-09 Baxter International Inc. Systems for separating high hematocrit red blood cell concentrations
US5783085A (en) 1982-12-13 1998-07-21 Estate Of William F. Mclaughlin Blood fractionation method
US5792351A (en) 1996-09-26 1998-08-11 The United States Of America As Represented By The Secretary Of The Navy Spinning filter separation system for oil spill clean-up operation
EP0885619A1 (en) 1997-06-16 1998-12-23 Terumo Kabushiki Kaisha Blood component collecting apparatus
US5906589A (en) 1996-11-13 1999-05-25 Cobe Laboratories, Inc. Method and apparatus for occlusion monitoring using pressure waveform analysis
US5919125A (en) 1997-07-11 1999-07-06 Cobe Laboratories, Inc. Centrifuge bowl for autologous blood salvage
US5964724A (en) 1996-01-31 1999-10-12 Medtronic Electromedics, Inc. Apparatus and method for blood separation
US5980760A (en) 1997-07-01 1999-11-09 Baxter International Inc. System and methods for harvesting mononuclear cells by recirculation of packed red blood cells
US6007725A (en) 1991-12-23 1999-12-28 Baxter International Inc. Systems and methods for on line collection of cellular blood components that assure donor comfort
US6059979A (en) 1991-12-23 2000-05-09 Baxter International Inc. Blood processing systems and methods using apparent hematocrit as a process control parameter
EP1057534A1 (en) 1999-06-03 2000-12-06 Haemonetics Corporation Centrifugation bowl with filter core
US6234989B1 (en) 1995-06-07 2001-05-22 Gambro, Inc. Extracorporeal blood processing methods and apparatus
US6251284B1 (en) * 1995-08-09 2001-06-26 Baxter International Inc. Systems and methods which obtain a uniform targeted volume of concentrated red blood cells in diverse donor populations
US6296602B1 (en) 1999-03-17 2001-10-02 Transfusion Technologies Corporation Method for collecting platelets and other blood components from whole blood
US20010027156A1 (en) 1999-06-03 2001-10-04 Yair Egozy Core for blood processing apparatus
US20020120227A1 (en) 2000-02-10 2002-08-29 Childers Robert Warren Method and apparatus for monitoring and controlling peritoneal dialysis therapy
US20020128582A1 (en) * 2001-03-06 2002-09-12 Liam Farrell Automated system and method for pre-surgical blood donation and fluid replacement
US20020156464A1 (en) * 2001-03-01 2002-10-24 Brian Blischak Non-constant pressure infusion pump
US20030055375A1 (en) 1999-12-17 2003-03-20 Holst Peter A. Method for compensating for pressure differences across valves in cassette type IV pump
EP1295619A2 (en) 2001-09-19 2003-03-26 Terumo Kabushiki Kaisha Platelet collection apparatus
US20030175150A1 (en) 1998-03-13 2003-09-18 Grimm Daniel J. Apheresis system with anticoagulant flow control
US6623443B1 (en) 1999-01-14 2003-09-23 Hans-Dietrich Polaschegg Method and device for the detection of stenosis in extra-corporeal blood treatment
US20030216683A1 (en) * 2001-11-26 2003-11-20 Nili-Med Ltd. Drug delivery device and method
US20030229302A1 (en) * 1998-10-16 2003-12-11 Mission Medical, Inc. Blood processing system
US6743192B1 (en) * 1998-09-11 2004-06-01 Koichiro Sakota Apheresis apparatus and method for producing blood products
US20040147865A1 (en) * 1994-10-13 2004-07-29 Cianci James P. System and method for processing blood
US20040186409A1 (en) 2003-01-28 2004-09-23 Gambro Dasco S.P.A. Apparatus and method for monitoring a vascular access of a patient subjected to an extracorporeal blood treatment
CN2735985Y (en) 2004-09-10 2005-10-26 上海达华医疗器械有限公司 Disposable blood cell separating device
US20060155236A1 (en) 2004-12-21 2006-07-13 Stephen Gara Method and apparatus for collecting a blood component and performing a photopheresis treatment
US20070078370A1 (en) * 2005-06-13 2007-04-05 Smith & Nephew, Inc. *Ew* Surgical Fluid Management
US7270645B2 (en) 1992-07-10 2007-09-18 Gambro Bct, Inc Apparatus for producing blood component products
US20080146993A1 (en) 2006-12-19 2008-06-19 Cytyc Corporation Systems and Methods for Drug Infusion with Feedback Control
US20080275377A1 (en) * 2005-05-18 2008-11-06 Gambro Lundia Ab Apparatus for Controlling Blood Flow in an Extracorporeal Circuit
US20090259164A1 (en) 2008-04-14 2009-10-15 Etienne Pages System and Method for Optimized Apheresis Draw and Return
US7704454B1 (en) 2003-10-08 2010-04-27 Caridianbct, Inc. Methods and devices for processing blood

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS596952A (en) 1982-07-02 1984-01-14 Hitachi Koki Co Ltd Rotary seal structure for flowing sample into rotary container and discharging the same therefrom
JPS5969166A (en) 1982-10-13 1984-04-19 Nikkiso Co Ltd Centrifugal separating bowl
EP0165254A1 (en) 1983-12-13 1985-12-27 Baxter Travenol Laboratories, Inc. Flexible disposable centrifuge system
JPH0657250B2 (en) 1984-06-29 1994-08-03 バクスター・インターナショナル・インコーポレーテッド Blood flow control device for blood extraction and reinfusion
IT1217938B (en) 1988-06-28 1990-03-30 Girolamo Sirchia Prepn. and storage of platelet concentrates from buffy-coats
JP2558509B2 (en) * 1988-08-12 1996-11-27 株式会社ニッショー Plasma collection device
US5186431A (en) 1989-09-22 1993-02-16 Yehuda Tamari Pressure sensitive valves for extracorporeal circuits
JPH0775746B2 (en) 1991-10-11 1995-08-16 株式会社矢口鉄工所 Lifter plate for lifting the can body
WO1994006535A1 (en) 1992-09-11 1994-03-31 Halbert Fischel Apparatus and method for fractionating a liquid mixture
JP3715338B2 (en) 1994-11-11 2005-11-09 テルモ株式会社 Blood component separator
EP1847283B1 (en) 1995-04-18 2010-07-14 CaridianBCT, Inc. Particle separation method
JPH09192215A (en) 1996-01-17 1997-07-29 Takaharu Nakane Centrifugal bowl
DE19917197C1 (en) * 1999-04-16 2000-07-27 Fresenius Medical Care De Gmbh Method to determine blood flow in vessel entrance of haemodialysis unit; involves measuring arterial and venous pressures when vessel entrance is open to allow blood flow and closed to prevent blood flow
MXPA02002500A (en) * 2000-07-07 2004-09-10 Baxter Int Medical system, method and apparatus employing mems.
DE102006032815A1 (en) * 2006-07-14 2008-01-17 Fresenius Medical Care Deutschland Gmbh Method and device for monitoring extracorporeal blood circulation

Patent Citations (195)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1025059A (en) 1911-02-24 1912-04-30 Joseph Eleuterio Hatton Process of centrifugal separation.
US1611725A (en) 1925-05-07 1926-12-21 Maskin Och Brobyggnads Ab Clarifier
US2087778A (en) 1936-01-07 1937-07-20 Kone Ja Silta O Y Maskin Och B Centrifugal machine for filtering purposes
US2661150A (en) 1947-12-17 1953-12-01 Jr William G Abbott Centrifuge
US2750107A (en) 1952-10-02 1956-06-12 Glacier Co Ltd Centrifugal oil cleaner, including a cylindrical filter
US2792172A (en) 1953-03-03 1957-05-14 Glacier Co Ltd Centrifugal filters
US3096283A (en) 1959-06-24 1963-07-02 Becton Dickinson Co Container for blood and machine for separating precipitates from liquid blood constituents
US3244362A (en) 1959-06-24 1966-04-05 George N Hein Centrifuging apparatus and fractionating system
US3244363A (en) 1959-06-24 1966-04-05 George N Hein Centrifuge apparatus and bag therefor
US3239136A (en) 1962-05-07 1966-03-08 George N Hein Centrifuge and centrifuge head for separating constituents of a liquid and a liner therefor
US3145713A (en) 1963-09-12 1964-08-25 Protein Foundation Inc Method and apparatus for processing blood
US3489145A (en) 1966-08-08 1970-01-13 Surgeon General Of The Public Method and apparatus for continuous separation of blood in vivo
US3456875A (en) 1966-08-18 1969-07-22 George N Hein Air driven centrifuge
US3409213A (en) 1967-01-23 1968-11-05 500 Inc Rotary seal and centrifuge incorporation
US3565330A (en) 1968-07-11 1971-02-23 Cryogenic Technology Inc Rotary seal and centrifuge incorporating same
US3655058A (en) 1970-07-13 1972-04-11 Richard A Novak Filtration apparatus
US3737096A (en) 1971-12-23 1973-06-05 Ibm Blood processing control apparatus
US3774840A (en) 1972-01-17 1973-11-27 Environs Dev Inc Centrifugal separator
US4082217A (en) 1973-08-27 1978-04-04 Separex Sa Centrifuge apparatus
FR2258898A1 (en) 1974-01-29 1975-08-22 Heraeus Christ Gmbh
US3987961A (en) 1974-01-29 1976-10-26 Heraeus-Christ Gmbh Centrifuge bag for treatment of biological liquids
US4056224A (en) 1975-03-27 1977-11-01 Baxter Travenol Laboratories, Inc. Flow system for centrifugal liquid processing apparatus
US4014497A (en) 1975-04-22 1977-03-29 Escher Wyss Limited Vertical centrifuge
US4040965A (en) 1975-07-03 1977-08-09 Firma Supraton Aurer & Zucker Ohg Rotary filter separator
US4007871A (en) 1975-11-13 1977-02-15 International Business Machines Corporation Centrifuge fluid container
US4010894A (en) 1975-11-21 1977-03-08 International Business Machines Corporation Centrifuge fluid container
US4734089A (en) 1976-05-14 1988-03-29 Baxter Travenol Laboratories, Inc. Centrifugal blood processing system
US4086924A (en) 1976-10-06 1978-05-02 Haemonetics Corporation Plasmapheresis apparatus
US4140268A (en) 1977-03-15 1979-02-20 Haemo-Transfer S.A. Centrifugating device for biological liquids, having a rotatable container, and supporting bracket therefor
US4197847A (en) 1977-03-31 1980-04-15 Isaac Djerassi Method and apparatus for collecting transfusable granulocytes
SU660718A1 (en) 1977-04-25 1979-05-05 Специальное Конструкторское Бюро Биофизической Аппаратуры Robot for separating blood and flushing the heavier fraction
US4430072A (en) 1977-06-03 1984-02-07 International Business Machines Corporation Centrifuge assembly
US5217427A (en) 1977-08-12 1993-06-08 Baxter International Inc. Centrifuge assembly
US5217426A (en) 1977-08-12 1993-06-08 Baxter International Inc. Combination disposable plastic blood receiving container and blood component centrifuge
US4934995A (en) 1977-08-12 1990-06-19 Baxter International Inc. Blood component centrifuge having collapsible inner liner
US4387848A (en) 1977-10-03 1983-06-14 International Business Machines Corporation Centrifuge assembly
US4151844A (en) 1977-11-11 1979-05-01 Baxter Travenol Laboratories, Inc. Method and apparatus for separating whole blood into its components and for automatically collecting one component
US4142670A (en) 1978-01-27 1979-03-06 Beckman Instruments, Inc. Chylomicron rotor
US4321921A (en) 1978-08-17 1982-03-30 Solco Basel Ag Apparatus for sucking blood out of body cavities
SU762982A1 (en) 1978-09-22 1980-09-15 Sp K B Biofizicheskoj Apparatu Rotor for blood separation and washing heavy fraction
US4303193A (en) 1979-01-22 1981-12-01 Haemonetics Corporation Apparatus for separating blood into components thereof
US4285464A (en) 1979-01-22 1981-08-25 Haemonetics Corporation Apparatus for separation of blood into components thereof
GB2047110A (en) 1979-03-28 1980-11-26 Hoegman Claes Folke Separating blood components
US4300717A (en) 1979-04-02 1981-11-17 Haemonetics Corporation Rotary centrifuge seal
US4466888A (en) 1980-05-20 1984-08-21 Haemonetics Corporation Suction liquid collection assembly and flexible collecting bag therefor
US4457747A (en) 1980-05-30 1984-07-03 Tu Ho C Exchange transfusion machine
US4425114A (en) 1981-04-23 1984-01-10 Haemonetics Corporation Blood donation unit
US4464167A (en) 1981-09-03 1984-08-07 Haemonetics Corporation Pheresis apparatus
US4687580A (en) * 1982-01-11 1987-08-18 Rhone-Poulenc S.A. Membrane apparatus/process adapted for plasmapheresis
US4447221A (en) 1982-06-15 1984-05-08 International Business Machines Corporation Continuous flow centrifuge assembly
US4482342A (en) 1982-06-17 1984-11-13 Haemonetics Corporation Blood processing system for cell washing
US4680025A (en) 1982-08-24 1987-07-14 Baxter Travenol Laboratories, Inc. Blood component collection systems and methods
US4490135A (en) 1982-09-24 1984-12-25 Extracorporeal Medical Specialties, Inc. Single needle alternating blood flow system
US5783085A (en) 1982-12-13 1998-07-21 Estate Of William F. Mclaughlin Blood fractionation method
SU1146098A1 (en) 1983-05-11 1985-03-23 Специальное Конструкторское Бюро Биофизической Аппаратуры Rotor for separating blood and washing heavy fractions
EP0128683A2 (en) 1983-05-26 1984-12-19 BAXTER INTERNATIONAL INC. (a Delaware corporation) Single needle blood fractionation system having adjustable recirculation through filter
US4655742A (en) * 1983-07-13 1987-04-07 Rhone-Poulenc S.A. Process/apparatus for the withdrawal/return of body fluids
US4530691A (en) 1983-12-13 1985-07-23 Baxter Travenol Laboratories, Inc. Centrifuge with movable mandrel
US4876013A (en) 1983-12-20 1989-10-24 Membrex Incorporated Small volume rotary filter
US5194145A (en) 1984-03-21 1993-03-16 William F. McLaughlin Method and apparatus for separation of matter from suspension
US5738792A (en) 1984-03-21 1998-04-14 Baxter International Inc. Method for separation of matter from suspension
US4534863A (en) 1984-05-22 1985-08-13 Schleicher & Schuell, Inc. Centrifugal filtering device and filter unit therefor
EP0171749A1 (en) 1984-08-07 1986-02-19 TERUMO KABUSHIKI KAISHA trading as TERUMO CORPORATION Apparatus for separating blood plasma, and apparatus therefor
US4911833A (en) 1984-08-24 1990-03-27 William F. McLaughlin Closed hemapheresis system and method
US4740202A (en) 1984-10-12 1988-04-26 Haemonetics Corporation Suction collection device
US4806247A (en) 1985-04-12 1989-02-21 Baxter International Inc. Plasmapheresis system and method
US4713176A (en) 1985-04-12 1987-12-15 Hemascience Laboratories, Inc. Plasmapheresis system and method
EP0208061A1 (en) 1985-05-14 1987-01-14 Biotest Pharma GmbH Method and device for obtaining blood plasma
US4643714A (en) 1985-08-05 1987-02-17 Cobe Laboratories, Inc. Single needle apparatus
US4740313A (en) 1985-08-12 1988-04-26 Baxter Travenol Laboratories, Inc. Method of filtering using a rotating and oscillating spinner
US4869812A (en) 1985-08-12 1989-09-26 Baxter International Inc. Disposable diagnostic plasma filter dispenser
US4684361A (en) 1985-10-11 1987-08-04 Cardiovascular Systems, Inc. Centrifuge
US4795419A (en) 1985-10-11 1989-01-03 Kardiothor, Inc. Centrifuge
US4692136A (en) 1985-10-11 1987-09-08 Cardiovascular Systems Inc. Centrifuge
US4647279A (en) 1985-10-18 1987-03-03 Cobe Laboratories, Inc. Centrifugal separator
US4808307A (en) 1985-12-23 1989-02-28 Haemonetics Corporation Couette membrane filtration apparatus for separating suspended components in a fluid medium using high shear
US4871462A (en) 1985-12-23 1989-10-03 Haemonetics Corporation Enhanced separation of blood components
US4755300A (en) 1985-12-23 1988-07-05 Haemonetics Corporation Couette membrane filtration apparatus for separating suspended components in a fluid medium using high shear
US4708712A (en) 1986-03-28 1987-11-24 Cobe Laboratories, Inc. Continuous-loop centrifugal separator
US5098372A (en) 1986-04-24 1992-03-24 Stafilum Ab Methods and machine based on blood separation by filtration for plasma exchange treatment, plasma donation and cytapheresis such as platelet apheresis
US5147290A (en) 1986-04-24 1992-09-15 Stafilum Ab Method and machine based on the principle of centrifugation for cytapheresis such as platelet apheresis, and for plasma exchange treatment
EP0257755A1 (en) 1986-07-22 1988-03-02 Haemonetics Corporation Centrifuge bowl or rotor for plasmapheresis
US4943273A (en) 1986-07-22 1990-07-24 Haemonetics Corporation Disposable centrifuge bowl for blood processing
US4983158A (en) 1986-07-22 1991-01-08 Haemonetics Corporation Plasmapheresis centrifuge bowl
US4795448A (en) 1986-08-08 1989-01-03 Haemonetics Corporation Suction collection system
US4968295A (en) 1986-09-22 1990-11-06 Fresenius Ag Method of separating the constituents of the blood
US4940543A (en) 1987-01-30 1990-07-10 Baxter International Inc. Plasma collection set
US5656163A (en) 1987-01-30 1997-08-12 Baxter International Inc. Chamber for use in a rotating field to separate blood components
US4806252A (en) 1987-01-30 1989-02-21 Baxter International Inc. Plasma collection set and method
US4767396A (en) 1987-03-03 1988-08-30 Haemonetics Corporation Method and apparatus for processing biological fluids
US5174894A (en) 1987-06-25 1992-12-29 Terumo Kabushiki Kaisha Blood component separation apparatus
US4850995A (en) 1987-08-19 1989-07-25 Cobe Laboratories, Inc. Centrifugal separation of blood
US4889524A (en) 1987-09-04 1989-12-26 Haemonetics Corporation Portable centrifuge apparatus
US5114396A (en) 1987-09-15 1992-05-19 Omega Medicinteknik Ab Method of washing blood cells and container assembly thereof
US4994188A (en) 1988-02-05 1991-02-19 Baxter International Inc. Adaptive filtrate flow control system using controlled reduction in filter efficiency
US4985153A (en) 1988-06-23 1991-01-15 Asahi Medical Co., Ltd. Method for separating blood into blood components, and blood components separator unit
US5484396A (en) 1988-11-17 1996-01-16 Naficy; Sadeque S. Method and device for treatment of HIV infections and AIDS
US5300060A (en) 1989-06-12 1994-04-05 Miles Inc. Blood bag system for separation and isolation of neocytes and gerocytes
US4983156A (en) 1989-07-03 1991-01-08 Benjamin Knelson Centrifugal separator
US5098373A (en) 1989-07-19 1992-03-24 Fresenius Ag Process for controlling blood pumps in the extra-corporeal circuit of a single needle arrangement and apparatus thereof
US5100372A (en) 1990-03-02 1992-03-31 Haemonetics Corporation Core for blood processing apparatus
US5045048A (en) 1990-03-29 1991-09-03 Haemonetics Corporation Rotary centrifuge bowl and seal for blood processing
US5039401A (en) 1990-05-16 1991-08-13 Eastman Kodak Company Blood collection and centrifugal separation device including a valve
US5234403A (en) 1990-05-25 1993-08-10 Sumitomo Bakelite Co., Ltd. Blood collecting apparatus
US5135667A (en) 1990-06-14 1992-08-04 Baxter International Inc. Method and apparatus for administration of anticoagulant to red cell suspension output of a blood separator
US5112298A (en) 1990-06-25 1992-05-12 Baxter International Inc. Apheresis method and device
US5254248A (en) 1990-06-28 1993-10-19 Terumo Kabushiki Kaisha Blood plasma separating apparatus
US5462667A (en) 1990-10-05 1995-10-31 Pall Corporation Filter for liquor filtration
US5141486A (en) 1990-11-05 1992-08-25 Cobe Laboratories, Inc. Washing cells
US5141486B1 (en) 1990-11-05 1996-01-30 Cobe Lab Washing cells
US5154716A (en) 1990-11-06 1992-10-13 Miles Inc. Bottom blood bag separation system
US5100564A (en) 1990-11-06 1992-03-31 Pall Corporation Blood collection and processing system
US5318511A (en) 1991-02-06 1994-06-07 Hospal Industrie Method and apparatus for controlling the circulation of blood in a single needle circuit
US5273517A (en) 1991-07-09 1993-12-28 Haemonetics Corporation Blood processing method and apparatus with disposable cassette
US5298171A (en) 1991-08-09 1994-03-29 Fresenius Ag Method and apparatus for separation of blood into its components
US5318512A (en) 1991-09-06 1994-06-07 Fresenius Ag Blood separation device
US5277701A (en) 1991-11-15 1994-01-11 Regents Of The University Of Minnesota Treatment of aluimmunization and refractoriness to platelet transfusion by protein A column therapy
US6059979A (en) 1991-12-23 2000-05-09 Baxter International Inc. Blood processing systems and methods using apparent hematocrit as a process control parameter
US6207063B1 (en) 1991-12-23 2001-03-27 Baxter International Inc. Blood processing systems and methods using apparent hematocrit as a process control parameter
US6007725A (en) 1991-12-23 1999-12-28 Baxter International Inc. Systems and methods for on line collection of cellular blood components that assure donor comfort
US5298016A (en) 1992-03-02 1994-03-29 Advanced Haemotechnologies Apparatus for separating plasma and other wastes from blood
US5417650A (en) 1992-03-02 1995-05-23 Advanced Haemotechnologies Apparatus for separating plasma and other wastes from blood
US5403272A (en) 1992-05-29 1995-04-04 Baxter International Inc. Apparatus and methods for generating leukocyte free platelet concentrate
US5649903A (en) 1992-05-29 1997-07-22 Baxter International Inc. Apparatus and methods for generating leukocyte free platelet concentrate
EP0578086A1 (en) 1992-06-30 1994-01-12 Terumo Kabushiki Kaisha Apparatus and method for transferring separated components in liquid
US7270645B2 (en) 1992-07-10 2007-09-18 Gambro Bct, Inc Apparatus for producing blood component products
US5665061A (en) 1992-08-11 1997-09-09 Cobe Laboratories, Inc. Biological/pharmaceutical method and apparatus for collecting and mixing fluids
US5386734A (en) 1992-08-21 1995-02-07 Fresenius Ag Centrifuge system for the separation of blood into its components
US5543062A (en) 1992-10-07 1996-08-06 Asahi Medical Co., Ltd. Leukocyte-removing filter device and system and method of using thereof
US5405308A (en) 1992-10-13 1995-04-11 Haemonetics Corporation Disposable centrifuge rotor and core for blood processing
US5387187A (en) 1992-12-01 1995-02-07 Haemonetics Corporation Red cell apheresis method
US5368555A (en) 1992-12-29 1994-11-29 Hepatix, Inc. Organ support system
US5368542A (en) 1993-01-13 1994-11-29 Cobe Laboratories, Inc. Apparatus and method for separating microscopic units in a substantially continuous density gradient solution
US5316540A (en) 1993-01-13 1994-05-31 Cobe Laboratories Apparatus and method for separating microscopic units in a substantially continuous density gradient solution
US5387174A (en) 1993-01-29 1995-02-07 Elp Rochat Centrifugal separator with disposable bowl assembly
US5470483A (en) 1993-03-22 1995-11-28 Hospal Industrie Device and method for controlling the balance of fluids in an extracorporeal blood circuit
EP0619145A2 (en) 1993-04-05 1994-10-12 Electromedics, Inc. Rotary seal for centrifuge
US5607579A (en) 1993-04-27 1997-03-04 Haemonetics Corporation Apheresis apparatus for separating an intermediate density component from whole blood
US5494592A (en) 1993-04-27 1996-02-27 Haemonetics Corporation Apheresis apparatus and method
US5437624A (en) 1993-08-23 1995-08-01 Cobe Laboratories, Inc. Single needle recirculation system for harvesting blood components
US5551941A (en) 1993-10-14 1996-09-03 E. I. Du Pont De Nemours And Company Automatic sample container handling centrifuge and a rotor for use therein
EP0654277A1 (en) 1993-10-21 1995-05-24 Cobe Laboratories, Inc. Blood component collection system with optimizer
US5431814A (en) 1993-10-22 1995-07-11 Jorgensen; Glen Centrifugal filter apparatus and method
US5514070A (en) 1994-01-21 1996-05-07 Haemonetics Corporation Plural collector centrifuge bowl for blood processing
US5505685A (en) 1994-01-21 1996-04-09 Cobe Laboratories Automation of plasma sequestration
US5437598A (en) 1994-01-21 1995-08-01 Cobe Laboratories, Inc. Automation of plasma sequestration
EP0664159A1 (en) 1994-01-21 1995-07-26 Haemonetics Corporation Plural collector centrifuge bowl for blood processing
US20040147865A1 (en) * 1994-10-13 2004-07-29 Cianci James P. System and method for processing blood
US5733253A (en) 1994-10-13 1998-03-31 Transfusion Technologies Corporation Fluid separation system
US5733446A (en) 1994-12-02 1998-03-31 Bristol-Myers Squibb Company Centrifuge with annular filter
US5585007A (en) 1994-12-07 1996-12-17 Plasmaseal Corporation Plasma concentrate and tissue sealant methods and apparatuses for making concentrated plasma and/or tissue sealant
US5733545A (en) 1995-03-03 1998-03-31 Quantic Biomedical Partners Platelet glue wound sealant
US5728060A (en) 1995-06-07 1998-03-17 Transfusion Technologies Corporation Blood collection and separation system
US5779660A (en) 1995-06-07 1998-07-14 Transfusion Technologies Corporation Blood collection and separation process
US6234989B1 (en) 1995-06-07 2001-05-22 Gambro, Inc. Extracorporeal blood processing methods and apparatus
US5651766A (en) 1995-06-07 1997-07-29 Transfusion Technologies Corporation Blood collection and separation system
US6251284B1 (en) * 1995-08-09 2001-06-26 Baxter International Inc. Systems and methods which obtain a uniform targeted volume of concentrated red blood cells in diverse donor populations
US5762791A (en) 1995-08-09 1998-06-09 Baxter International Inc. Systems for separating high hematocrit red blood cell concentrations
US5643193A (en) * 1995-12-13 1997-07-01 Haemonetics Corporation Apparatus for collection washing and reinfusion of shed blood
US5964724A (en) 1996-01-31 1999-10-12 Medtronic Electromedics, Inc. Apparatus and method for blood separation
EP0799645A1 (en) 1996-04-03 1997-10-08 Haemonetics Corporation Centrifuge bowl for blood processing
US5882289A (en) 1996-04-03 1999-03-16 Haemonetics Corporation Centrifuge bowl with improved core structure
US5792351A (en) 1996-09-26 1998-08-11 The United States Of America As Represented By The Secretary Of The Navy Spinning filter separation system for oil spill clean-up operation
US5906589A (en) 1996-11-13 1999-05-25 Cobe Laboratories, Inc. Method and apparatus for occlusion monitoring using pressure waveform analysis
EP0885619A1 (en) 1997-06-16 1998-12-23 Terumo Kabushiki Kaisha Blood component collecting apparatus
US5980760A (en) 1997-07-01 1999-11-09 Baxter International Inc. System and methods for harvesting mononuclear cells by recirculation of packed red blood cells
US5919125A (en) 1997-07-11 1999-07-06 Cobe Laboratories, Inc. Centrifuge bowl for autologous blood salvage
US20030175150A1 (en) 1998-03-13 2003-09-18 Grimm Daniel J. Apheresis system with anticoagulant flow control
US6743192B1 (en) * 1998-09-11 2004-06-01 Koichiro Sakota Apheresis apparatus and method for producing blood products
US6817984B2 (en) * 1998-10-16 2004-11-16 Mission Medical, Inc. Blood processing system
US20030229302A1 (en) * 1998-10-16 2003-12-11 Mission Medical, Inc. Blood processing system
US6623443B1 (en) 1999-01-14 2003-09-23 Hans-Dietrich Polaschegg Method and device for the detection of stenosis in extra-corporeal blood treatment
US6296602B1 (en) 1999-03-17 2001-10-02 Transfusion Technologies Corporation Method for collecting platelets and other blood components from whole blood
US6558307B2 (en) 1999-03-17 2003-05-06 Haemonetics Corporation Method for collecting platelets and other blood components from whole blood
US20010027156A1 (en) 1999-06-03 2001-10-04 Yair Egozy Core for blood processing apparatus
US6464624B2 (en) 1999-06-03 2002-10-15 Haemonetics Corporation Blood processing method and apparatus using a centrifugation bowl with filter core
EP1057534A1 (en) 1999-06-03 2000-12-06 Haemonetics Corporation Centrifugation bowl with filter core
US20050235733A1 (en) 1999-12-17 2005-10-27 Holst Peter A Method for compensating for pressure differences across valves in cassette type IV pump
US20030055375A1 (en) 1999-12-17 2003-03-20 Holst Peter A. Method for compensating for pressure differences across valves in cassette type IV pump
US6497676B1 (en) 2000-02-10 2002-12-24 Baxter International Method and apparatus for monitoring and controlling peritoneal dialysis therapy
US20020120227A1 (en) 2000-02-10 2002-08-29 Childers Robert Warren Method and apparatus for monitoring and controlling peritoneal dialysis therapy
US20020156464A1 (en) * 2001-03-01 2002-10-24 Brian Blischak Non-constant pressure infusion pump
US20020128582A1 (en) * 2001-03-06 2002-09-12 Liam Farrell Automated system and method for pre-surgical blood donation and fluid replacement
US20030066807A1 (en) 2001-09-19 2003-04-10 Atsushi Suzuki Platelet collection apparatus
EP1295619A2 (en) 2001-09-19 2003-03-26 Terumo Kabushiki Kaisha Platelet collection apparatus
US20030216683A1 (en) * 2001-11-26 2003-11-20 Nili-Med Ltd. Drug delivery device and method
US20040186409A1 (en) 2003-01-28 2004-09-23 Gambro Dasco S.P.A. Apparatus and method for monitoring a vascular access of a patient subjected to an extracorporeal blood treatment
US20070112289A1 (en) 2003-01-28 2007-05-17 Gambro Lundia Ab Apparatus and method of monitoring a vascular access of a patient subjected to an extracorporeal blood treatment
US7704454B1 (en) 2003-10-08 2010-04-27 Caridianbct, Inc. Methods and devices for processing blood
CN2735985Y (en) 2004-09-10 2005-10-26 上海达华医疗器械有限公司 Disposable blood cell separating device
US20060155236A1 (en) 2004-12-21 2006-07-13 Stephen Gara Method and apparatus for collecting a blood component and performing a photopheresis treatment
US20080275377A1 (en) * 2005-05-18 2008-11-06 Gambro Lundia Ab Apparatus for Controlling Blood Flow in an Extracorporeal Circuit
US20070078370A1 (en) * 2005-06-13 2007-04-05 Smith & Nephew, Inc. *Ew* Surgical Fluid Management
US20080146993A1 (en) 2006-12-19 2008-06-19 Cytyc Corporation Systems and Methods for Drug Infusion with Feedback Control
US20090259164A1 (en) 2008-04-14 2009-10-15 Etienne Pages System and Method for Optimized Apheresis Draw and Return

Non-Patent Citations (18)

* Cited by examiner, † Cited by third party
Title
European Patent Office, International Search Report-Application No. PCT/US2009/040199, dated Sep. 10, 2009 (15 pages), including Written Opinion of the International Searching Authority.
European Patent Office, International Search Report—Application No. PCT/US2009/040199, dated Sep. 10, 2009 (15 pages), including Written Opinion of the International Searching Authority.
Japanese Patent Office Final Official Action (Final Decision for Rejection)-Application No. 2011-504,203, dated Oct. 4, 2013 (2 pages) [English Translation].
Japanese Patent Office Final Official Action (Final Decision for Rejection)—Application No. 2011-504,203, dated Oct. 4, 2013 (2 pages) [English Translation].
Japanese Patent Office Final Official Action-Application No. 2011-504,203, dated Oct. 4, 2013 (2 pages).
Japanese Patent Office Final Official Action—Application No. 2011-504,203, dated Oct. 4, 2013 (2 pages).
Japanese Patent Office, First Official Action (Notification of Reason for Rejection)-Application No. 2011-504,203, dated Jun. 4, 2013 (4 pages) [English Translation].
Japanese Patent Office, First Official Action (Notification of Reason for Rejection)—Application No. 2011-504,203, dated Jun. 4, 2013 (4 pages) [English Translation].
Japanese Patent Office, Official Action-Application No. 2011-504,203, dated Jun. 4, 2013 (3 pages).
Japanese Patent Office, Official Action—Application No. 2011-504,203, dated Jun. 4, 2013 (3 pages).
The State Intellectual Property Office of the People's Republic of China Second Official Action-Application No. 200980119781.3, dated Oct. 15, 2013 (13 pages) [English Translation].
The State Intellectual Property Office of the People's Republic of China Second Official Action—Application No. 200980119781.3, dated Oct. 15, 2013 (13 pages) [English Translation].
The State Intellectual Property Office of the People's Republic of China Second Official Action-Application No. 200980119781.3, dated Oct. 15, 2013 (9 pages).
The State Intellectual Property Office of the People's Republic of China Second Official Action—Application No. 200980119781.3, dated Oct. 15, 2013 (9 pages).
The State Intellectual Property Office of the People's Republic of China, First Official Action (Notification of the First Office Action)-Application No. 2009801197813, dated Nov. 26, 2012 (10 pages) [English Translation].
The State Intellectual Property Office of the People's Republic of China, First Official Action (Notification of the First Office Action)—Application No. 2009801197813, dated Nov. 26, 2012 (10 pages) [English Translation].
The State Intellectual Property Office of the People's Republic of China, First Official Action-Application No. 2009801197813, dated Nov. 26, 2012 (8 pages).
The State Intellectual Property Office of the People's Republic of China, First Official Action—Application No. 2009801197813, dated Nov. 26, 2012 (8 pages).

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9486590B2 (en) 2014-09-29 2016-11-08 Fenwal, Inc. Automatic purging of air from a fluid processing system
US9498567B2 (en) 2014-09-29 2016-11-22 Fenwal, Inc. Systems and methods for controlling the return phase of a blood separation procedure
US10220132B2 (en) 2014-12-19 2019-03-05 Fenwal, Inc. Biological fluid flow control apparatus and method
US12078630B2 (en) 2018-01-05 2024-09-03 Path Ex, Inc. Device for the capture and removal of disease material from fluids
US20210205734A1 (en) * 2019-06-06 2021-07-08 Pneumatic Scale Corporation Centrifuge System for Separating Cells in Suspension
US11957998B2 (en) * 2019-06-06 2024-04-16 Pneumatic Scale Corporation Centrifuge system for separating cells in suspension
US20240261708A1 (en) * 2019-06-06 2024-08-08 Pneumatic Scale Corporation Centrifuge System for Separating Cells in Suspension

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